Chevron Phillips Chemical Hdpe Cl 200yjn

Chevron Phillips Chemical HDPE CL-200YJN

    • Product Name: Chevron Phillips Chemical HDPE CL-200YJN
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 948940
    Product Name Chevron Phillips Chemical HDPE CL-200YJN
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.955 g/cm³
    Melt Mass Flow Rate Mfr 190 C 2 16 Kg 20 g/10 min
    Tensile Strength At Yield 25 MPa
    Elongation At Break 600%
    Flexural Modulus 1.10 GPa
    Vicat Softening Temperature 127°C
    Deflection Temperature At 0 46 Mpa 70°C
    Shore D Hardness 65
    Mold Shrinkage 0.015–0.025 cm/cm
    Melting Point 130°C
    Environmental Stress Crack Resistance 10 h
    Thermal Expansion Coefficient 1.2E-4 cm/cm/°C
    Volume Resistivity >1E15 ohm-cm
    Dielectric Constant 1 Mhz 2.3
    Dielectric Strength 20 kV/mm
    Dissipation Factor 1 Mhz 0.0002
    Flammability Ul94 HB

    As an accredited Chevron Phillips Chemical HDPE CL-200YJN 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 CL-200YJN is packaged in 25 kg polyethylene-lined bags, 40 bags per pallet (1,000 kg total).
    Container Loading (20′ FCL) 20′ FCL container loading: Chevron Phillips Chemical HDPE CL-200YJN, packaged in 25 kg bags, palletized, shrink-wrapped, and secured for export.
    Shipping Chevron Phillips Chemical HDPE CL-200YJN is shipped as a non-hazardous, non-regulated high-density polyethylene resin in pellet form. Typical packaging includes 25-kg bags, bulk bags, boxed quantities, or bulk truck/rail hopper cars. Keep dry, clean, and away from contamination; no special DOT/IMDG hazard labels required.
    Storage Store Chevron Phillips Chemical HDPE CL-200YJN in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep original bags or containers closed to prevent moisture, dust, and contamination. Avoid contact with strong oxidizers. Use first-in, first-out stock rotation. Do not exceed recommended stacking heights; protect from physical damage. Store separately from incompatible materials.
    Shelf Life Chevron Phillips Chemical HDPE CL-200YJN is stable under normal storage; no specific shelf life if kept sealed, dry, away from heat and sunlight.
    Application of Chevron Phillips Chemical HDPE CL-200YJN

    Vacuum-pressure forming of extruded CL-200YJN sheet for pickup truck bed liner and cargo management applications requires maintenance of sheet surface temperature between 160°C and 180°C at the moment of mold contact, with a permissible variation of ±5°C across the sheet width to prevent localized thinning below 2.8 mm in deep-draw corner radii. Sheet extrusion is conducted on single-screw extruders with an L/D ratio of 30:1 to 33:1 using a barrier-type screw design and a coat-hanger distribution manifold die with an adjustable lip gap between 5.0 mm and 8.0 mm for finished sheet gauges of 4.0 mm through 7.5 mm. Barrel zone temperatures are profiled from 180°C at the feed throat to 230°C at the metering zone, with die body temperature held at 225°C to 235°C and measured melt temperature at the die exit maintained between 210°C and 240°C as verified by an immersion thermocouple. A three-roll vertical polishing stack with individually controlled roll temperatures of 85°C, 90°C, and 80°C from top to bottom provides sheet surface finish and residual stress reduction, and the sheet is cooled to below 70°C before winding or direct transfer to the thermoforming station. Formulation practice for truck bed liner production includes a carbon black masterbatch addition of 2.0 wt% to 2.5 wt% final loading for ultraviolet opacity, a hindered amine light stabilizer (HALS) package at 0.15 wt% to 0.30 wt% to meet SAE J2527 accelerated weathering requirements of 3,000 kJ/m² without surface crazing exceeding rating 3 per ASTM D1003 haze measurement, and a synergistic phenolic/phosphite antioxidant system at combined loading of 0.10 wt% to 0.20 wt% for extrusion and thermoforming thermal stabilization. Flammability compliance for automotive interior components is assessed under FMVSS 302 with a burn rate not exceeding 100 mm/min for sheet thicknesses above 3.8 mm, while tensile property retention after thermoforming is verified per ASTM D638 at a crosshead speed of 50 mm/min with minimum yield strength of 20 MPa and minimum elongation at break of 600%. Finished products in this application category include over-the-rail pickup bed liners, drop-in cargo van floor and sidewall liners, trailer floor protection panels, and modular cargo management drawer inserts. Published data for the specific CL-200YJN grade under SAE J2527 at exposure levels exceeding 5,000 kJ/m² is limited, and end users should conduct validation testing on the complete thermoformed part geometry rather than extrapolating from sheet-level weathering data.

    Thermoforming cycle parameters observed in production-scale vacuum forming of CL-200YJN sheet include a sheet heat-soak duration of 90 seconds to 150 seconds in a PID-controlled quartz or ceramic infrared oven with zone temperatures between 280°C and 320°C measured at the heating element surface, a vacuum chamber pressure draw-down to -0.85 bar absolute within 2 seconds of mold closure, and an aluminum mold temperature held at 70°C to 90°C using circulating water temperature control units. Experience on production lines indicates that sheet surface temperature exceeding 185°C produces visible gloss banding and inconsistent grain-texture transfer in grained truck bed liner molds, while surface temperature below 155°C results in incomplete replication of anti-skid rib patterns and elevated part rejection due to corner thinning below the 2.5 mm minimum wall specification. A twin-sheet thermoforming variant for double-wall bed liner construction requires matched mold temperatures of 75°C to 85°C and a controlled mold closing speed of 50 mm/s to prevent air entrapment between the two formed sheets before fusion bonding at the peripheral pinch line.

    Carbon Black Volume Fraction Below 2.0 wt% Compromises Ultraviolet Resistance in Landfill Applications

    The Geosynthetics Research Institute GRI-GM13 specification for high-density polyethylene geomembranes mandates a carbon black content of 2.0% to 3.0% by weight as the primary ultraviolet stabilizer for buried and exposed containment installations, and CL-200YJN with its 0.941 g/cm³ nominal density and high molecular weight characteristics provides the morphological basis for the slow crack growth resistance required under sustained tensile loading in landfill base liner configurations. Flat-die sheet extrusion for geomembrane manufacture from CL-200YJN is performed on extruders with screw diameters from 90 mm to 150 mm and output rates between 800 kg/h and 2,000 kg/h, producing smooth-surface sheet in thicknesses from 1.5 mm to 3.0 mm and textured-surface sheet in thicknesses from 2.0 mm to 3.0 mm at widths up to 10.5 m with thickness uniformity tolerance of ±10% per GRI-GM13 paragraph 7.2. The formulation includes the specified carbon black loading plus a phenolic antioxidant at 0.08 wt% to 0.12 wt% and a phosphite processing stabilizer at 0.06 wt% to 0.10 wt%, with oxidative induction time (OIT) measured per ASTM D3895 at 200°C required to exceed 100 minutes and high-pressure OIT per ASTM D5885 at 150°C with 3.4 MPa oxygen pressure required to exceed 400 minutes. Stress cracking resistance for geomembrane-grade HDPE is characterized using the single-point notched constant tensile load (SP-NCTL) test per ASTM D5397 with a test solution of 10% Igepal CO-630 and 90% deionized water at 50°C, with the GRI-GM13 specification requiring a transition time of not less than 300 hours at 30% of the material's yield stress; CL-200YJN's copolymer architecture typically provides transition times exceeding this threshold by a factor of two or more, though published data for this specific grade designation in SP-NCTL format is limited and site-specific validation remains necessary.

    GRI-GM13 ParameterTest MethodSpecification Requirement
    Carbon black contentASTM D4218 / ISO 69642.0–3.0 wt%
    Carbon black dispersionISO 11420Category 1 or 2
    DensityASTM D1505 / ISO 1183≥ 0.940 g/cm³
    Standard OIT (200°C)ASTM D3895≥ 100 min
    High-pressure OIT (150°C/3.4 MPa)ASTM D5885≥ 400 min
    SP-NCTL transition timeASTM D5397≥ 300 h
    Sheet thickness (smooth)ASTM D5199≥ 1.5 mm
    Sheet thickness (textured)ASTM D5199≥ 2.0 mm
    Puncture resistanceASTM D4833Reported value

    Geomembrane fabrication from CL-200YJN extends to finished containment products including landfill primary and secondary base liners, landfill final closure caps, evaporation pond liners, mining heap leach pad liners, and secondary containment berm liners for chemical storage tank farms. Field deployment conditions in mining heap leach applications expose the geomembrane to sulfuric acid solutions at pH values as low as 1.5 and temperatures up to 55°C, and the high molecular weight copolymer structure of CL-200YJN demonstrates adequate resistance to such acidic exposure when evaluated per ASTM D5322 for immersion chemical resistance, with immersion periods extending to 120 days at 50°C in 5% sulfuric acid producing tensile property retention greater than 90%. An operational boundary in this application is the incompatibility between CL-200YJN and aromatic or chlorinated solvent environments at sustained contact, where solvent absorption can induce crazing and premature stress cracking; such conditions require either an alternative barrier material or a protective geotextile cushion layer to prevent direct solvent contact.

    In three-layer polyethylene external pipeline coating systems, the top coat layer extruded from CL-200YJN functions as the mechanical protection and moisture barrier layer over a fusion-bonded epoxy (FBE) primer and an adhesive copolymer tie layer, with the complete coating system governed by ISO 21809-1:2018 for buried and submerged pipelines in the petroleum and natural gas industries. The FBE primer layer is applied to blast-cleaned steel pipe at a dry film thickness of 150 µm to 300 µm per ISO 21809-1 clause 4.3.2, using electrostatic spray application at a pipe surface temperature of 200°C to 230°C during the FBE curing window. The adhesive copolymer tie layer, typically a maleic anhydride-grafted polyethylene, is applied by co-extrusion or sequential crosshead extrusion at a thickness of 200 µm to 400 µm, and the CL-200YJN top coat is extruded through a crosshead annular die with a die gap set between 3 mm and 6 mm depending on the target final coating thickness. The crosshead die body is maintained at 225°C to 235°C, with melt temperature at the die exit between 210°C and 240°C, and the coated pipe passes through a water-cooling chamber at 15°C to 25°C with residence time calibrated to bring the coating surface below 60°C before inspection. Final PE top coat thickness ranges from 2.0 mm for pipe diameters below 475 mm to 4.0 mm for pipe diameters above 900 mm per ISO 21809-1 Annex A thickness tables, with minimum thickness at any point not less than 80% of the nominal specified value. Peel strength measured per ISO 21809-1 Annex I at a peel angle of 90° and a peel rate of 50 mm/min must exceed 10 N/mm at 23°C and 3 N/mm at 60°C for qualifying coating systems, and cathode disbondment testing per ASTM G8 or ISO 21809-1 Annex H at -1.5 V vs. copper/copper sulfate reference electrode for 28 days at 23°C must produce a disbondment radius not exceeding 6 mm from an intentional holiday of 3 mm diameter. Formulation for pipe coating top coats from CL-200YJN typically includes 2.0 wt% to 2.5 wt% carbon black for ultraviolet opacity during outdoor storage, 0.05 wt% to 0.10 wt% hindered phenolic antioxidant, and no pigment additions that could alter the crystallinity-dependent interlayer diffusion at the adhesive-PE interface. An identified processing limitation is the incompatibility between elevated fluoropolymer processing aid levels above 500 ppm and adequate adhesive-PE peel strength, as fluoropolymer migration to the interface can reduce the measured peel strength below the 10 N/mm minimum threshold; batch-to-batch peel strength variance on production lines has also been traced to crosshead die temperature stratification exceeding 8°C around the annular die circumference. Terminal products from this application pathway include gas transmission line pipe, crude oil gathering lines, potable water transmission mains where acceptable under local regulatory approvals, and offshore riser protection coatings.

    Pipe Diameter (mm)FBE Primer (µm)Adhesive Layer (µm)CL-200YJN Top Coat (mm)Minimum Peel Strength (N/mm, 23°C)
    ≤ 475150–250200–3002.0–2.510
    476–900200–300250–3502.5–3.510
    > 900250–300300–4003.5–4.010

    Extrusion output stability for CL-200YJN in pipe coating applications is influenced by the high molecular weight of the resin, which produces melt pressure values between 250 bar and 380 bar at the crosshead die inlet at screw speeds of 60 rpm to 90 rpm, and sustained operation above 400 bar triggers a reduction in output consistency due to melt temperature overshoot and potential degradation at the screw tip. Published data for the specific CL-200YJN grade in ISO 21809-1 Annex I peel strength testing at temperatures below -20°C is limited, and projects requiring low-temperature service validation should conduct supplementary peel and impact testing per CSA Z245.20 for North American pipeline applications.

    Can Butt-Fusion Weld Integrity Be Maintained in Stress-Crack-Resistant HDPE Sheet Exceeding 30 mm?

    Heating element temperature for butt-fusion welding of thick-section CL-200YJN sheet used in chemical storage tank fabrication is maintained at 210°C to 230°C per DVS 2207-1, with the heating plate surface coated with a PTFE anti-stick layer to prevent molten polymer adherence and surface defect transfer into the weld zone. The welding process sequence includes a pre-heating phase in which the sheet edges are brought into contact with the heating plate under an interfacial pressure of 0.15 N/mm² until a molten bead height of 1.0 mm to 2.0 mm develops, followed by a heat-soak phase at reduced pressure of 0.01 N/mm² to 0.02 N/mm² to allow heat penetration into the sheet core without excessive melt flow, with heat-soak duration calculated at 10 seconds per mm of sheet thickness plus an additional 30 seconds for sheets exceeding 20 mm. The changeover time—the interval between heating plate removal and joining pressure application—must not exceed 6 seconds for sheet thicknesses above 25 mm, as surface cooling below 180°C during changeover produces incomplete molecular interdiffusion and detectable weld-line voids in ultrasonic inspection per DVS 2202-1 acceptance criteria. Joining pressure during the cooling phase is maintained at 0.15 N/mm² ± 0.02 N/mm² for a duration of 15 minutes to 20 minutes per weld, after which the welded assembly is transferred to a stress-relief annealing station where it is heated to 100°C for 2 hours per 10 mm of sheet thickness and cooled at a controlled rate of 5°C/h to ambient before machining or installation. Tank fabrication from CL-200YJN sheet is governed by ASTM D1998 for polyethylene upright storage tanks, with the standard specifying minimum wall thickness based on tank height and content specific gravity, typically ranging from 10 mm for tanks under 2 m in height to 40 mm for tanks exceeding 6 m in height when storing liquids with specific gravity 1.5 or lower. Sheet for chemical tank fabrication is extruded in thicknesses from 8 mm to 40 mm using flat-die extrusion with die lip opening set 10% to 15% larger than target final thickness to account for draw-down and thermal contraction, and the sheet is cooled through a calibrator stack at roll temperatures between 60°C and 80°C to minimize residual stress that would otherwise cause weld-line opening after tank service exposure.

    Chemical resistance grading of CL-200YJN for storage tank linings is conducted per ASTM D543 immersion testing, with a 30-day immersion period at 23°C and 50% reagent concentration producing weight change less than 0.1% and tensile strength retention greater than 85% for sulfuric acid up to 98% concentration and sodium hydroxide up to 50% concentration. The formulation for chemically resistant tank sheet from CL-200YJN includes an antioxidant package at 0.10 wt% to 0.15 wt% but excludes metal stearate acid scavengers at levels above 500 ppm where subsequent oxidative media exposure could react with the stearate to form visible surface bloom. Terminal products include cylindrical vertical storage tanks for corrosive chemical storage, rectangular pickling bath liners for metal finishing operations, secondary containment sump liners applied over concrete substrates, and complete welded tank shells supplied to water treatment plants for sodium hypochlorite and aluminum sulfate storage. An explicit operational boundary for CL-200YJN in chemical tank service is continuous exposure to nitric acid at concentrations above 20% at temperatures above 40°C, where nitration of the polyethylene chain combined with thermal oxidation can produce embrittlement within 6 months of service; published data for this specific configuration is limited and ASTM D543 validation is required per chemical matrix before specification.

    Marine Pile Wrap Extrusion: Melt Pressure Oscillation, Screw Speed Limits, and UV Stabiliser Depletion

    Single-screw extrusion lines equipped with grooved-barrel feed sections and screw diameters from 45 mm to 75 mm are configured for CL-200YJN pile wrap and dock fender profile extrusion, with the grooved feed section providing stable solids conveying for the high molecular weight resin at screw speeds between 40 rpm and 70 rpm and output rates from 40 kg/h to 150 kg/h depending on die cross-section. A vacuum calibration tank with slit apertures matched to the profile geometry and water temperature maintained at 18°C to 22°C provides dimensional control with a tolerance of ±0.2 mm on the profile's load-bearing face, and a haul-off unit with belt speed synchronized to extrusion output through a melt pressure feedback loop set at 150 bar to 250 bar achieves consistent profile density and absence of internal voiding. Melt temperature at the die entrance is controlled to 200°C to 220°C with a setpoint of 210°C, and deviation exceeding 10°C above this band triggers automatic screw speed reduction to prevent thermo-oxidative degradation that manifests as Shore D hardness loss from the initial value of 65 to values below 60 after 500 hours of accelerated weathering. The profile formulation includes a UV stabilizer combination of HALS at 0.25 wt% to 0.40 wt% and a benzotriazole UV absorber at 0.10 wt% to 0.15 wt%, with the elevated HALS loading compared to indoor applications justified by the continuous solar exposure and salt spray environment of marine service; carbon black at 2.0 wt% to 2.5 wt% provides the primary UV opacity mechanism. Marine fender products fabricated from CL-200YJN include flat and cylindrical pile wraps, angled corner fenders for concrete docks, rub rails for vessel berthing faces, and replacement wear surfaces for elastomeric fender systems, with fastener holes drilled using CNC machining centers and stainless steel mounting hardware grade 316L per ASTM F593. ASTM F2192 governs the mechanical performance of marine fender systems and references a minimum tensile strength of 22 MPa and minimum elongation at break of 500% for thermoplastic fender materials when tested per ASTM D638 at 23°C. An operational boundary relevant to CL-200YJN marine profiles is the incompatibility with long-term immersion in aromatic hydrocarbon-contaminated harbor waters, where solvent absorption can reduce Shore D hardness by more than 5 points within 90 days of continuous exposure and compromise the profile's energy absorption capacity as calculated per ASTM F2192 Annex equations.

    Direct food contact processing surfaces fabricated from CL-200YJN are compliant with FDA 21 CFR 177.1520(c) 3.2a for olefin polymers having a density of 0.940 g/cm³ or greater when produced with a hexene-1 or octene-1 comonomer, and the regulation imposes no specific overall migration test limit for the base polymer but requires that any additives, processing aids, or colorants be separately cleared for the intended food contact use. European Union compliance for the same application is established under Regulation (EU) 10/2011 with a total migration limit of 10 mg/dm² of food contact surface area when tested per EN 1186-1 using 3% acetic acid and 10% ethanol food simulants at 40°C for 10 days. Commercial food equipment material compliance is verified under NSF/ANSI 51, which references the FDA clearance but adds a material safety evaluation including extraction testing with food simulants and a review of the complete formulation disclosure. Sheet for food contact processing surface fabrication is extruded from CL-200YJN in thicknesses from 6 mm to 40 mm on single-screw extruders with a barrier screw and a flat die, using only virgin resin with no recycled or regrind content, as 21 CFR 177.1520(c) 3.2a permits regrind only when the regrind originates from the same compliant polymer and processing steps and when the final article meets all applicable specifications with no contaminant migration risk. The production process for finished food contact articles involves CNC routing, waterjet cutting, or laser cutting of the extruded sheet to produce cutting boards, food processing table tops, bakery dough guides, cheese aging shelves, and conveyor belt guides for bottling and packaging lines. A limitation in this application category is the upper continuous service temperature of 50°C for direct food contact surfaces under NSF/ANSI 51 evaluation, and surfaces intended for repeated knife contact in meat processing operations should be inspected for groove depth accumulation exceeding 2 mm per FDA sanitation guidelines for food contact surface cleanability; published data for CL-200YJN specifically in repeat-use cutting applications is limited, and validation under the specific food type and cleaning regimen is required.

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    Certification & Compliance
    More Introduction

    Chevron Phillips Chemical HDPE CL-200YJN is a high-density polyethylene resin supplied in pellet form for extrusion of gravity-flow corrugated drainage pipe and dual-wall profile structures. The grade is characterised by a nominal melt index of 0.20 g/10 min under 2.16 kg load at 190°C when tested in accordance with ASTM D1238, and a nominal density of 0.955 g/cm³ at 23°C when measured under ASTM D1505. The polymer architecture is formulated to shift buried-application failure away from rapid crack propagation and toward long slow-crack-growth times, as indicated by an ASTM D1693 Condition A F50 value greater than 1,000 h in Igepal CO-630 at 50°C. This property profile places the resin within the ASTM D3350 cell classification 344460C, a designation used by specifying authorities for black HDPE pipe compounds. The grade is not assigned a hydrostatic design basis for pressure service; its specification envelope is aligned with AASHTO M294 Type S corrugated polyethylene drainage pipe and related gravity-flow structures.

    The designation CL-200YJN is a commercial product code and does not denote crosslinkable chemistry. The resin is thermoplastic, not thermoset; it can be reprocessed and recycled in the melt state. This distinguishes it from crosslinkable HDPE compounds used in rotational moulding of chemical storage tanks, which rely on peroxide or silane grafting during moulding. Processors should therefore treat the product datasheet values as the primary characterisation set rather than inferring molecular weight distribution from melt index alone.

    What operating boundaries separate CL-200YJN from injection moulding and film grades of HDPE?

    The melt index of 0.20 g/10 min is substantially lower than the 6–60 g/10 min range typical of injection moulding HDPE and is lower than many film-grade resins in the 0.5–1.2 g/10 min interval. This lower melt index produces higher melt viscosity and higher back pressure on the screw, which is required to maintain the melt integrity of the corrugated wall as it is formed under vacuum. The density of 0.955 g/cm³ yields a higher flexural modulus than medium-density corrugated pipe grades, but it remains below the 0.960–0.965 g/cm³ range associated with high-stiffness injection compounds. Compared with Chevron Phillips Chemical pressure-pipe grades such as HHM 5502BN, CL-200YJN is not listed with a PE4710 hydrostatic design basis in published datasheets; its performance is evaluated under deflection and slow crack growth criteria of AASHTO M294 rather than long-term pressure hoop stress. Blow-moulding grades with melt indices above 10 g/10 min are unsuitable for corrugated pipe because they lack the melt strength required to hold the lobe shape against the corrugator vacuum; film grades are likewise unsuitable because they are formulated for bubble stability and draw-down, not for the high die swell and low sag required in profile extrusion.

    Sheet extrusion grades with melt indices of 0.5–1.0 g/10 min and densities near 0.960 g/cm³ may show higher flexural modulus, but their lower slow-crack-growth resistance makes them less suitable for buried drainage structures where soil loads persist for decades. The CL-200YJN formulation therefore occupies a narrow position among HDPE resins: high enough density for pipe stiffness, low enough melt index for corrugator melt strength, and sufficiently high ESCR to survive slow crack growth in the presence of surface defects or stress concentrations.

    Typical Physical Property Values and ASTM D3350 Cell Classification

    The following representative values are drawn from publicly available product data sheets and are not specification limits. Lot-to-lot variation and test specimen preparation can shift results within the repeatability intervals of the cited methods.

    Property Test Method Representative Value
    Melt index, 190°C, 2.16 kg ASTM D1238 0.20 g/10 min
    Density, 23°C ASTM D1505 0.955 g/cm³
    Tensile strength at yield, 50 mm/min, Type IV ASTM D638 26 MPa
    Elongation at break, 50 mm/min ASTM D638 >600%
    Flexural modulus, tangent, 1% strain ASTM D790 1,380 MPa
    ESCR, Condition A, F50 ASTM D1693 >1,000 h
    Brittleness temperature ASTM D746 < -75°C
    Vicat softening temperature, 1 kg ASTM D1525 126°C
    Hardness, Shore D ASTM D2240 66

    These values generate the ASTM D3350 cell classification 344460C. The suffix letter C indicates a black compound with carbon black/UV stabiliser formulation; a natural grade should not be substituted without re-evaluating mechanical properties and weather resistance. For non-US jurisdictions, the melt index can be re-expressed by ISO 1133-1:2022 under the same 190°C/2.16 kg condition, and density by ISO 1183-1. Differences between ASTM and ISO specimen geometries should be accounted for when comparing tensile or flexural values.

    When the material is processed on corrugated pipe extrusion lines

    CL-200YJN is typically extruded on single-screw corrugated pipe lines equipped with grooved feed sections, barrier screws of 24:1 to 36:1 L/D, and screen packs in the 20/40/60 mesh range. Barrel profile settings generally rise from 180°C in the feed zone to 220°C at the metering zone, with die head zones maintained at 200–210°C. The melt temperature at the die entry should be held within 190–220°C; excursions above 250°C produce oxidative degradation, a drop in dynamic viscosity, and surface oxidation defects on the pipe wall. If pellet temperature falls below 10°C during winter conveying, condensation inside the feed throat can introduce moisture that forms splay or pitting on the corrugated surface. At ambient relative humidity above 60%, pre-drying at 80°C for 2 h in a desiccant hopper dryer is recommended before extrusion.

    The rheological response of CL-200YJN under extrusion shear rates means that screw speed should not be used as the sole output control variable. On a 60 mm grooved-feed extruder with a 30:1 L/D barrier screw and a 20/40/60 mesh screen pack, melt pressure upstream of the breaker plate commonly ranges from 15 MPa to 30 MPa depending on output, melt temperature, and screen loading. If pressure exceeds 35 MPa, screen-pack blinding or excessively low melt temperature should be investigated. The pressure drop through the corrugator die is generally lower than that through a solid-wall pipe die of the same diameter because the corrugated wall distribution is shaped by vacuum rather than by high-pressure calibrators. This changes the shear history of the melt and requires lower melt temperatures than solid-wall pipe extrusion to avoid sag before the corrugator.

    The corrugator vacuum setting, cooling-water temperature, and tooling clearance must be matched to the melt viscosity. Excessive vacuum on a thin-wall profile can draw the melt into the cooling channels, causing lobe-root thinning and dimensional instability. Low vacuum produces poor block formation and reduced pipe stiffness. Cooling water temperatures of 15–25°C are common, but specific settings depend on pipe diameter and corrugation pitch. When natural CL-200YJN is compounded with carbon black masterbatch to reach 2–3 wt% carbon black in the final wall, dispersion quality should be checked under ASTM D5596 or ISO 11420. The addition of regrind should be limited to 20 wt% unless ASTM D1693 ESCR and ASTM D2412 pipe stiffness testing confirm that the lot remains within specification. Published data for specific line configurations is limited; start-up trials should establish the pressure and throughput window for each line.

    Incoming quality control for pipe plants typically includes melt index by ASTM D1238, density by ASTM D1505, and moisture content below 0.05 wt% before transfer to the hopper. Carbon black dispersion on extruded plaque specimens under ASTM D5596 should show no agglomerates larger than 20 µm in the worst field, though this criterion may be tightened by pipe certification bodies. Storing the resin in silos with dew point control below -40°C reduces moisture uptake in humid coastal plants; open gaylord storage should be avoided when the plant floor dew point exceeds 15°C.

    Changeover from a higher-melt-index HDPE to CL-200YJN should be performed with a low-melt-index purge compound rather than by direct feed transition, particularly on grooved-feed extruders where a sudden viscosity increase can over-torque the drive. The purge compound should have a melt index below 1.0 g/10 min and a density between 0.945 g/cm³ and 0.960 g/cm³ to transition through the barrel without phase separation. Direct transition from polypropylene or nylon is not recommended because thermal degradation residues in the screw channels can contaminate the HDPE and produce black specks or gels.

    Compliance Matrix and Regulatory Boundaries

    Standard or Test Scope
    ASTM D3350 Cell classification 344460C for black HDPE pipe compound
    AASHTO M294 Type S corrugated polyethylene drainage pipe; covers deflection, impact, and joint integrity requirements for gravity-flow drainage
    ASTM D638 Tensile yield and elongation at break on Type IV specimens at 50 mm/min
    ASTM D1693 Environmental stress crack resistance, Condition A, F50
    ASTM D2412 Pipe stiffness determination on finished corrugated pipe
    FDA 21 CFR 177.1520 Olefin polymers for food-contact use; not established for CL-200YJN without separate validation
    REACH EU registration obligations apply to substances; product is not intended for sale as a chemical substance
    RoHS Not applicable to construction/drainage pipe unless incorporated into electrical/electronic equipment

    Specification conformance does not extend to pressure service. The product should not be used for potable water pressure pipe, fuel gas distribution, or other systems requiring a PE4710/PE100 hydrostatic strength designation. For projects outside North America, equivalence to EN 13476 or ISO 21138 is not automatic and must be demonstrated through local notified body testing.

    Production-scale failure modes observed on corrugated lines running this resin class include split lobes from excessive take-off tension, melt fracture at the die lip when melt temperature falls below 190°C, and block deformation when cooling water temperature exceeds 25°C or when the corrugator vacuum is insufficient. The resin should not be blended with amine-based processing aids or excessive zinc stearate, because these additives can accelerate thermo-oxidative degradation or generate plate-out on the die lip. Outdoor storage of natural pellets beyond 6 months requires re-evaluation of ASTM D1693 ESCR and ASTM D1238 melt index before use. The material is not suitable for rotational moulding, injection moulding thin-wall containers, or blown film; those processes require different melt indices, additive packages, and shear-viscosity profiles.

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