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Lianyungang Petrochemical HDPE STL 7260

    • Product Name: Lianyungang Petrochemical HDPE STL 7260
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 378685
    Product Lianyungang Petrochemical HDPE STL 7260
    Polymertype High-density polyethylene (HDPE)
    Grade STL 7260
    Pipeclassification PE100
    Minimumrequiredstrength 10 MPa
    Density 0.958 g/cm³ (23°C)
    Meltflowrate 0.23 g/10 min (190°C/5 kg)
    Tensileyieldstrength ≥25 MPa
    Elongationatbreak ≥600%
    Flexuralmodulus ≥1000 MPa
    Notchedimpactstrength ≥20 kJ/m²
    Vicatsofteningtemperature ≥120°C
    Oxidationinductiontime ≥20 min
    Carbonblackcontent 2.0-2.5%
    Environmentalstresscrackresistance ≥5000 h
    Color Black
    Form Pellets

    As an accredited Lianyungang Petrochemical HDPE STL 7260 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Lianyungang Petrochemical HDPE STL 7260 is supplied in 25 kg woven bags, 40 bags per pallet (1,000 kg net).
    Container Loading (20′ FCL) 20′ FCL container loaded with 25 kg bags of Lianyungang Petrochemical HDPE STL 7260, palletized, shrink-wrapped, and stowed for export.
    Shipping Lianyungang Petrochemical HDPE STL 7260 is shipped as non-hazardous thermoplastic resin pellets in 25 kg PP woven bags, 500–1000 kg jumbo bags, or bulk lined containers. Transport in dry, clean trucks or containers at ambient temperature; protect from moisture, sunlight, and contamination. No special dangerous goods handling required.
    Storage Store Lianyungang Petrochemical HDPE STL 7260 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, ignition sources, and incompatible chemicals. Keep original bags or containers sealed, palletized, and off the floor. Prevent moisture, dust, oil, and static buildup. Stack securely within recommended height limits. Use first-in, first-out inventory. Follow the manufacturer’s SDS and local regulations.
    Shelf Life Properly stored in cool, dry, ventilated area in unopened original packaging, shelf life is typically 24 months from production date.
    Application of Lianyungang Petrochemical HDPE STL 7260

    Lianyungang Petrochemical HDPE STL 7260 enters the thin-wall food packaging sector through high-cavitation tools producing sidewalls below 1.0 mm and flow-path-to-thickness ratios commonly above 150:1. The process conflict in this application lies between the need for fast cavity filling to avoid premature freeze-off and the need for controlled hold-pressure decay to limit sink marks on the rim. A profiled injection speed is used. The screw starts at 20–40 mm/s for the first 10–15 mm of displacement, accelerates to 120–180 mm/s through the main filling phase, and decelerates to 30–60 mm/s before switch-over at 95–98 % of shot volume. Melt temperature is maintained in the 200–230 °C band, mould temperature at 10–25 °C, and hot-runner manifold temperature at 210–230 °C. Gate diameters of 0.5–1.0 mm and vent depths of 0.02–0.04 mm are typical for this wall-stock class. Cavity pressure during hold is normally held at 40–60 MPa until gate freeze. Prior to tooling simulation, the grade-specific melt mass-flow rate is read from the supplier certificate of analysis under ISO 1133-1:2022 at 190 °C/2.16 kg. A general-purpose polyolefin screw with an L/D ratio of 20:1–24:1 and a compression ratio of 2.5:1–3.5:1 is preferred. The check ring must limit back-flow to below 5 % of shot volume. Higher leakage causes shot-size drift and cavity-weight variation. The resin is not normally pre-dried when original sealed packaging is used. If storage humidity exceeds 60 % RH or visible surface condensation is present, hopper drying at 70–80 °C for 1–2 h prevents splay.

    Food-contact compliance in this sector is not a single additive statement. The resin must be assessed under FDA 21 CFR 177.1520 for olefin polymers, under EU Regulation (EU) No 10/2011 with overall migration measured according to EN 1186-1, and under GB 4806.6-2016 for articles sold into China. If a colour masterbatch is used, the let-down ratio is typically limited to 1–3 wt% and the masterbatch must comply with the same food-contact positive lists. Terminal articles produced in this sector include deli lids, dairy spread tubs, frozen dessert containers, and thin-wall snack cups.

    Does Gate Position or Wall Thickness Govern Weld-Line Strength in HDPE STL 7260 Crates?

    Industrial stack-nest crates and distribution totes made from HDPE STL 7260 operate in a different mechanical loading regime than thin-wall packaging. Wall thicknesses range from 3.5 mm to 6.0 mm. The main process conflict shifts from freeze-off to internal void formation and weld-line weakness. Weld lines in thick HDPE sections are dominated by the meeting angle of the melt fronts. Gate location is therefore adjusted so that the melt fronts meet at an angle of at least 75°. Lower meeting angles produce a persistent notch-like line. Field data from production-scale machines with clamp force between 600 t and 1200 t show that a poorly positioned gate can reduce weld-line tensile strength sufficiently to cause cracking during column stacking. Melt temperature is held at 180–220 °C, mould temperature at 15–35 °C, and hydraulic injection pressure between 70–100 MPa. Back pressure is maintained at 0.5–1.0 MPa to avoid screw-slip and to maintain melt homogenisation. The hold-pressure profile is staged. An initial high segment limits sink at the rib roots, followed by a lower segment until gate seal. Conformal cooling in the core reduces cycle time by 15–25 % compared with straight drilled channels. Part-weight variation across cavities should be kept below 0.5 % of shot weight.

    Regulatory requirements for this sector do not normally include food-contact certification unless the crate is used for direct unpackaged food. Compliance is instead anchored to REACH Regulation (EC) No 1907/2006 Annex XVII and SVHC screening, with additional RoHS Directive 2011/65/EU verification where crates enter electronics logistics. UV-stabilised outdoor crates incorporate a UV masterbatch at 2–5 wt%. Carbon black masterbatch is used at 2–3 wt% when long outdoor service is specified. Terminal articles include stack-nest crates, fruit and vegetable distribution crates, automotive parts bins, and bakery transport totes.

    Closure Dimensional Stability and Environmental Stress Cracking Resistance in HDPE STL 7260

    Closure manufacture is the most dimensionally constrained injection-moulding segment for HDPE STL 7260. Bottle neck inner diameters and tamper-evident band bridges require tolerances of ±0.05 mm or tighter on multi-cavity tools. High melt mass-flow rate assists filling of small gates in the 0.4–0.8 mm range. The same flow property can reduce environmental stress cracking resistance, which is a critical failure mode under top-load and wetting-agent contact. Processors therefore control the thermal history tightly. Melt temperature is maintained at 190–220 °C, mould temperature at 10–30 °C, and gate vestige thickness is kept below 0.1 mm on the closure top. Screw decompression is set to avoid drool without pulling air into the melt. ESCR is evaluated by ASTM D1693-15 Method B and, for notched fixed-load testing, by ISO 16770:2019. Child-resistant closures are additionally tested to ISO 8317:2015.

    Flip-top closures add a hinge section with local thickness variation. Packing pressure at the hinge must be held until gate freeze. Early pressure release produces sink marks and reduces hinge flexural fatigue life. Valve-gate sequencing on multi-cavity hot runners is used to balance fill, especially when cavity numbers exceed 32. The injection speed profile is deliberately slowed in the hinge area to avoid jetting across the cavity. Dimensional data are collected using laser gauging after conditioning for 24 h at 23 °C and 50 % relative humidity per ISO 291. Food-contact closure lots are verified under EU Regulation (EU) No 10/2011, FDA 21 CFR 177.1520, and GB 4806.6-2016. Regrind content above 15 wt% in closures must be qualified to maintain ESCR. Terminal articles include beverage caps, dairy closures, tamper-evident bands, and child-resistant pharmaceutical closures.

    Application segmentRegulatory basisTest method / clauseVerification focus
    Thin-wall food packagingFDA 21 CFR 177.1520, EU Regulation (EU) No 10/2011, GB 4806.6-2016EN 1186-1, EN 13130-1Overall migration, specific migration, organoleptic stability
    Caps and closuresFDA 21 CFR 177.1520, EU Regulation (EU) No 10/2011, ISO 8317:2015ASTM D1693-15, ISO 16770:2019, ISO 8317:2015ESCR, child-resistance, dimensional retention
    Toys and housewaresEN 71-3, ASTM F963-23, REACH Annex XVII entries 51–52EN 71-3, ISO 179-1Element migration, phthalate restriction, impact ductility
    Industrial pails and cratesREACH Regulation (EC) No 1907/2006, UN Model Regulations Chapter 6.1ISO 2248:2018, ASTM D1693-15Drop retention, ESCR, stacking stability
    Horticultural containersREACH Regulation (EC) No 1907/2006SVHC screeningHeavy-metal restriction, UV stabilizer migration

    When Wall-Stock Variation and Low-Temperature Impact Govern Toy and Houseware Moulding

    Toy and houseware moulds impose sudden changes in wall stock, long projected areas, and a need for low-temperature ductility. HDPE STL 7260 is processed at melt temperatures of 180–220 °C and mould temperatures of 15–40 °C. The injection speed is profiled to prevent jetting at the transition from a thin handle section to a thick base. A common profile uses a slow segment at 30–50 mm/s for the handle, followed by 80–120 mm/s in the main body. Hold pressure is limited to avoid overpacking thin ribs, which can warp on ejection. Colour masterbatches are restricted to lots pre-certified under EN 71-3 and ASTM F963-23. Phthalate-containing additive packages are excluded to satisfy REACH Regulation (EC) No 1907/2006 Annex XVII entries 51 and 52. Low-temperature performance is measured on notched Charpy specimens according to ISO 179-1. Published data for this specific configuration is limited, so validation on the production tool remains mandatory. Terminal articles include toy blocks, stacking cups, storage baskets, kitchen tool handles, and bath accessory components.

    Horticultural containers and propagation trays represent a separate downstream sector for HDPE STL 7260 in which the cycle-time target dominates processing decisions. Multi-cavity tools with cell walls below 1.5 mm require melt temperatures of 190–230 °C and mould temperatures of 10–30 °C. The injection speed is set high, typically 100–160 mm/s for the main filling segment, because the drainage-hole pins reduce the effective filling width and increase flow resistance. Back pressure is kept low at 0.3–0.8 MPa to avoid additive segregation. Outdoor-grade pots use a UV-stabilisation package at 2–4 wt%. Black or green masterbatches are selected for multi-season exposure. Ejection is aided by shallow draft angles and air ejection to prevent thin-wall deformation. The main quality parameter is part-weight consistency across cavities, which is controlled by monitoring cushion position and switch-over repeatability. Regulatory load is lower than food-contact sectors, but SVHC screening under REACH Regulation (EC) No 1907/2006 and heavy-metal limits in the masterbatch remain applicable. Terminal parts include nursery pots, plug trays, propagation trays, and hanging-basket saucers.

    Industrial Pail Moulding and Handle Retention in HDPE STL 7260

    Industrial pails from 5 L to 25 L combine a thin cylindrical sidewall with a thick rim and solid handle bosses. This produces a pronounced differential cooling profile. HDPE STL 7260 is moulded at melt temperatures of 180–220 °C, with mould temperatures of 15–35 °C and clamp forces between 400 t and 900 t. The injection profile is deliberately slowed during rim filling to avoid trapped gas at the handle-insert region. Hold pressure is staged to maintain dimensional roundness. Cooling fixtures are used after ejection until part temperature falls below 50 °C. Handle retention is not solely a material property. The boss geometry and insert design control failure mode. Drop testing is conducted per ISO 2248:2018, and stress-cracking resistance is screened with ASTM D1693-15 Method B. Dangerous-goods pails require testing under the UN Recommendations on the Transport of Dangerous Goods, Model Regulations, Chapter 6.1. Food-grade pails additionally require compliance with EU Regulation (EU) No 10/2011, FDA 21 CFR 177.1520, and GB 4806.6-2016. Terminal products include paint pails, adhesive pails, chemical pails, and food-ingredient pails.

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    Certification & Compliance
    More Introduction

    Lianyungang Petrochemical Co., Ltd. identifies HDPE STL 7260 as a high-density polyethylene resin for extruded pressure pipe and thick-section pipe fittings. The manufacturer’s technical bulletin lists a melt mass-flow rate of 0.22 g/10 min at 190 °C/5.0 kg per ISO 1133-1:2022 and a density of 0.959 g/cm³ per ISO 1183-1:2019. These values place the product in the low-MFR, high-melt-strength category of HDPE. General-purpose blow-molding and injection-molding HDPE grades with MFR above 2.0 g/10 min cannot be substituted in pressure-pipe service because they lack the long-term hydrostatic strength and slow crack growth resistance required by pipe system standards.

    The product is normally supplied as a black compound with carbon black content in the range 2.0–2.5 wt% measured by ISO 6964. Carbon black at this loading is not merely colorant; it functions as the ultraviolet-stabilization mechanism for outdoor storage and long-term buried service. The selected pellet geometry and bulk density are specified by the manufacturer for silo conveying and gravimetric dosing at pipe extrusion lines.

    The principal application is pressure-rated water distribution, industrial process water, and gas distribution pipe in the PE100 class. The grade is also used in thick-wall fittings where high integrity at butt-fusion joints is required. It is not intended for rotomolding, blown film, sheet, or thin-wall containers.

    What Are the Mechanical and Rheological Benchmarks?

    PropertyTypical valueTest standard
    Melt mass-flow rate0.22 g/10 min (190 °C/5.0 kg)ISO 1133-1:2022
    Density0.959 g/cm³ISO 1183-1:2019
    Tensile stress at yield25 MPaISO 527-2:2012
    Tensile elongation at break>600 %ISO 527-2:2012
    Flexural modulus1000 MPaISO 178:2019
    Charpy notched impact strength, 23 °C24 kJ/m²ISO 179-1/1eA
    Vicat softening temperature126 °CISO 306/A50
    Oxidation induction time at 210 °C>30 minISO 11357-6
    Carbon black content2.0–2.5 wt%ISO 6964
    Slow crack growth resistance>1000 hISO 13479:2009

    The melt mass-flow rate of 0.22 g/10 min is measured at 190 °C and 5.0 kg, not the 2.16 kg load used for high-flow HDPE. Comparing the two loads without correction is invalid. A low MFR under the heavier load indicates high melt viscosity, which helps prevent pipe-wall sag in large diameters but raises extruder torque. Density of 0.959 g/cm³ contributes to stiffness; flexural modulus of 1000 MPa is sufficiently high for standard SDR pressure ratings without requiring excessive wall thickness.

    Impact strength of 24 kJ/m² under ISO 179-1/1eA is a laboratory indicator of resistance to rapid crack propagation at ambient temperature. The notched-pipe value under ISO 13479:2009 at 80 °C and 4.0 MPa is more relevant to field performance because it introduces a sharp notch in the pipe wall and measures failure time. Oxidation induction time above 30 min at 210 °C provides a stability margin for start-up and short-term temperature excursions; it does not exempt processors from controlling melt residence time.

    The property profile is consistent with a high-molecular-weight pressure-pipe HDPE in which high-molecular-weight chains form tie molecules between crystalline lamellae. The low MFR indicates high weight-average molecular weight, while the broader molar-mass distribution improves shear thinning at pipe extrusion rates. A unimodal HDPE of similar density but without the high-molecular-weight fraction typically exhibits lower notched-pipe failure time under identical ISO 13479:2009 conditions. This structural difference is not visible in short-term tensile tests and must be confirmed by long-term pressure testing.

    When processed on a 65 mm grooved-feed single-screw extruder with 36:1 L/D and a barrier screw, a start-up barrel profile of 180–210 °C from feed zone to metering zone is typical. The die-head temperature is maintained at 205–215 °C, and the melt temperature at the screw tip is held between 200 °C and 220 °C. Melt pressure measured upstream of the screen changer normally remains below 35 MPa; extended operation above 35 MPa increases thrust-bearing load and shortens the stabilizer reserve. Screw speed on this equipment class is generally in the range 60–90 min⁻¹, but line output depends on pipe diameter, downstream cooling, and haul-off capacity.

    Pipe calibration and cooling require longer water-spray or vacuum-tank immersion than higher-MFR HDPE because the low melt flow reduces sag but also slows relaxation. For pipe outside diameters above 250 mm, internal cooling of the pipe is frequently necessary. A die land ratio of at least 10:1 is recommended to reduce melt fracture and obtain uniform wall thickness. Surface moisture is the primary inlet risk; if condensate exceeds 0.05 wt%, a 4 h dry-air purge at 80 °C removes surface water and prevents microvoids.

    Contamination from incompatible thermoplastics is a processing boundary. Polypropylene, PET, and polyamide particles above 2 wt% create hard domains that lower slow crack growth resistance and can delaminate the inner pipe wall under hydrostatic stress. Clean silo segregation and purging of transport lines are required when switching from a general-purpose high-MFR HDPE.

    When STL 7260 Replaces a Standard Unimodal HDPE in Pipe Coextrusion

    In contrast to a PE80 unimodal HDPE with an MFR of 0.5 g/10 min, STL 7260 creates higher die-head pressure at equal output. The increase can reach 10–20 % when the same die gap and screen pack are retained, requiring a reduction in screw speed of approximately 5–10 % or a wider die gap until the control system re-establishes the melt-pressure limit. The operational advantage is a wider processing window for thick-wall pipe: melt strength is sufficient to prevent sag in SDR 11 pipe above 315 mm outside diameter, provided the extruder has adequate torque.

    Compared with an injection-molding HDPE of MFR 20 g/10 min, STL 7260 is unsuitable for thin-wall injection molding. The spiral flow length under standard injection pressure is significantly lower; nominal wall sections below 2.5 mm are outside the recommended envelope. The differentiation is not a matter of product quality but of molecular design: pressure-pipe HDPE intentionally sacrifices ease of flow to preserve long-term creep resistance.

    Published data for this specific configuration is limited for comparison with PE100-RC grades that are formulated for additional slow crack growth resistance in unsettled trench conditions. The material achieves PE100 class but does not automatically carry the raised-resistance classification described for point-load service. Selection should not extrapolate beyond the manufacturer’s declared classification.

    Long-term hydrostatic design classification follows ISO 9080:2012 and ISO 12162:2009. A PE100 compound must demonstrate a lower prediction limit of hydrostatic strength at 20 °C and 50 years of at least 10 MPa. For water supply under ISO 4427:2019, the design coefficient C=1.25 converts MRS to an allowable design stress of 8.0 MPa. The pressure-rating formula MOP = 2 MRS / (C × (SDR − 1)) gives approximately 1.6 MPa for SDR 11 and 1.0 MPa for SDR 17 at 20 °C. These numerical relationships are the basis for sizing the product in water distribution systems.

    The central difference from PE80 is quantitative. A PE80 material with MRS 8.0 MPa must use a lower design stress; at equal outside diameter and pressure class, the PE80 wall is approximately 25 % thicker. STL 7260 therefore permits material reduction and lower hydraulic friction for a given pressure rating, provided the installation and operating temperature remain within the design assumptions.

    For a PE100 pipe at 1.0 MPa operating pressure and C=1.25, the minimum SDR is 17 because SDR = (2 MRS / (MOP × C)) + 1. At 1.6 MPa, the minimum SDR is 11. These calculations explain why STL 7260 is generally extruded in SDR 11 to SDR 17 dimensions for municipal water mains.

    For gaseous fuels under ISO 4437:2015, design coefficients vary by national code, but a factor C=2.0 is widely used. An SDR 11 pipe then corresponds to a maximum operating pressure of 1.0 MPa at 20 °C. The same PE100 compound may carry different MOP values depending on service fluid and authority.

    Batch-to-batch variance on industrial lines is controlled through melt-flow and density release testing. If the MFR drifts above 0.25 g/10 min, molecular weight is too low for the declared PE100 hydrostatic class; if density shifts below 0.955 g/cm³, ring stiffness falls at constant wall thickness. The manufacturer’s certificate of analysis typically reports melt mass-flow rate, density, carbon black content, and oxidation induction time for each production lot.

    Compliance Matrix, Handling Limitations, and Processing Boundaries

    The product is applicable to pipe systems specified under ISO 4427:2019 for water supply and ISO 4437:2015 for gaseous fuels, subject to national installation codes. Material not used within 12 months of delivery should be re-tested for oxidation induction time before extrusion. Storage at temperatures above 50 °C or in direct sunlight reduces stabilizer reserve; storage relative humidity above 80 % requires condensation protection on feed hoppers and silo vents.

    Standard or regulationScopeRelevant condition
    ISO 4427:2019Plastics piping systems for water supplyPE100 pressure service
    ISO 4437:2015Plastics piping systems for gaseous fuelsPE100 with national design factor
    ISO 1167-1:2006Hydrostatic strength testing20 °C/50 years extrapolation input
    ISO 13479:2009Notched pipe slow crack growth80 °C/4.0 MPa notched pipe
    ISO 9080:2012Plastics piping and ducting systemsLong-term hydrostatic regression
    ISO 12162:2009Classification of PE materialsMRS 10 MPa
    REACH 1907/2006Chemical safetyNo SVHC above 0.1 wt%
    RoHS 2011/65/EUHazardous substancesPb, Hg, Cd, Cr(VI), PBB, PBDE limits

    STL 7260 is not intended for blown film, sheet, or thin-wall injection molding. Mixing with post-industrial or post-consumer HDPE should be governed by the processor’s validated quality plan and may invalidate pressure-pipe certification if not permitted by the pipe standard. Avoid improvised blending with polypropylene, PET, or polyamide; even small quantities alter butt-fusion weld morphology and reduce slow crack growth margins. For buried gas distribution, the material’s hydrostatic design basis does not override installation-induced bending, squeeze-off damage, or third-party damage. The resin should not be processed outside the declared melt-temperature and melt-pressure limits, because thermal or shear overexposure depletes stabilizer reserve before visible surface defects appear.

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