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Shandong Yulong HDPE TR144

    • Product Name: Shandong Yulong HDPE TR144
    • 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 320660
    Polymertype High-density polyethylene (HDPE)
    Density 0.944–0.950 g/cm³
    Meltflowrate 0.20–0.30 g/10 min (190°C/5 kg)
    Tensileyieldstrength ≥23 MPa
    Elongationatbreak ≥600%
    Flexuralmodulus ≥900 MPa
    Vicatsofteningtemperature ≥120°C
    Brittlenesstemperature ≤-70°C
    Environmentalstresscrackingresistance ≥1000 h
    Oxidativeinductiontime ≥20 min at 200°C
    Carbonblackcontent 2.0–2.5%
    Waterabsorption <0.01%
    Hardness 60–65 Shore D
    Volumeresistivity ≥10^16 Ω·cm
    Dielectricstrength ≥20 kV/mm
    Thermalconductivity 0.4 W/(m·K)
    Coefficientoflinearthermalexpansion 1.2×10^-4 /°C
    Moisturecontent <0.1%

    As an accredited Shandong Yulong HDPE TR144 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Shandong Yulong HDPE TR144 is packed in 25 kg woven bags or 1,000 kg jumbo bags, palletized for transport.
    Container Loading (20′ FCL) 20′ FCL Container Loading: Shandong Yulong HDPE TR144, 25 kg bags, palletized, shrink-wrapped, 17 MT net, securely stowed for export.
    Shipping Shandong Yulong HDPE TR144 is a non-hazardous high-density polyethylene resin. It is typically shipped in 25 kg PP/PE bags or 500–1000 kg jumbo bags, palletized and stretch-wrapped. Transport in clean, dry containers, keeping it away from moisture, heat, and direct sunlight. Standard sea/land freight applies. Handle carefully to avoid bag damage.
    Storage Store Shandong Yulong HDPE TR144 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, ignition sources, and moisture. Keep original bags sealed and palletized off the floor. Avoid contact with oils, acids, bases, and strong oxidizers. Maintain clean, dust-free conditions, protect packaging from damage, and follow first-in, first-out stock rotation and local regulations.
    Shelf Life Shandong Yulong HDPE TR144: typically 24 months from manufacture when stored unopened in a cool, dry, ventilated area away from sunlight/heat.
    Application of Shandong Yulong HDPE TR144

    Extrusion of Shandong Yulong HDPE TR144 into T-shirt carrier sacks on high-output blown-film lines requires balancing calcium carbonate filler loadings against bubble stability, tear propagation resistance, and the onset of melt fracture at the die lip. On single-screw extruders with L/D 24:1–30:1 and air-cooled or IBC-equipped dies of 100–250 mm diameter, the melt temperature is maintained between 190 °C and 220 °C, the die gap is set at 1.0–1.5 mm, the blow-up ratio is held between 3:1 and 5:1, and the frost line height is positioned at 6–10 times the die diameter to produce films of 8–25 µm. The compounding formula is based on 100 phr HDPE TR144, with 5–25 phr of a calcium carbonate masterbatch containing 75–80 wt% CaCO3 in a polyolefin carrier, 2–6 phr of TiO2 white masterbatch, and 1–3 phr of a combined slip/antiblock masterbatch. At total CaCO3 loadings above 20 wt%, production lines exhibit bubble instability, die-lip deposit formation, and a measurable drop in Elmendorf tear resistance; the die gap is therefore widened above 1.5 mm to reduce shear stress and move the onset of melt fracture toward higher screw speeds. Compliance for non-food T-shirt sacks falls under EU Directive 94/62/EC and REACH (EC) No 1907/2006, while sacks used for unpackaged produce require olefin polymer compliance with FDA 21 CFR 177.1520(c) and EU Regulation 10/2011; mechanical verification is performed according to ISO 527-3, ISO 6383-2, and ISO 7765-1. Terminal products are T-shirt grocery sacks, produce bags, and point-of-sale merchandise bags.

    What Limits Down-Gauging in Heavy-Duty Sack Film?

    Down-gauging of HDPE TR144 heavy-duty refuse sacks is constrained less by burst strength than by regrind-induced gel formation and the loss of dart impact resistance at thicknesses below 30 µm. In extrusion runs at 30–80 µm, the base formulation is 100 phr HDPE TR144, 2–3 phr carbon black masterbatch to achieve 2.0–2.5 wt% carbon black, 0.2–0.5 phr hindered amine light stabilizer masterbatch, 0.05–0.1 phr calcium stearate acid scavenger, and 0.02–0.05 phr fluoroelastomer processing aid. Recovered edge trim from the same line is limited to ≤20 wt% of total feed; when post-industrial regrind exceeds this value, field data show an increase in gel count and a dart impact loss greater than 15% due to cumulative oxidative chain scission. The extrusion line uses high-stalk bubble geometry with internal bubble cooling, a die gap of 1.5–2.0 mm, a blow-up ratio from 2.5:1 to 4.0:1, and melt temperatures between 200 °C and 230 °C; outputs of 150–300 kg/h are typical on three-layer lines running mono-layer sacks. The primary production-scale failure is visible as gauge bands between ±8% and ±15% of nominal thickness when the air-ring velocity profile is not rebalanced after a change in blow-up ratio; these bands concentrate puncture and tear stress under load. Compliance verification for municipal waste sacks follows EN 13592, while dart impact is determined by ISO 7765-1 or ASTM D1709 and tensile properties by ISO 527-3. Terminal products include heavy-duty refuse sacks of 90–240 L, rubble sacks, and industrial bin liners.

    In three-layer coextruded barrier film for dry cereal packaging, HDPE TR144 is placed in the external and internal skins, while a polyamide or EVOH core is bonded by maleic anhydride-grafted tie layers. The skin-layer formulation consists of 100 phr HDPE TR144, erucamide slip at 500–1500 ppm, synthetic silica antiblock at 1000–2500 ppm, and a hindered phenol/phosphite antioxidant package at 0.05–0.15 wt%; calcium carbonate is omitted because it raises the seal initiation temperature and reduces the visual clarity of the internal sealant skin. The coextrusion line is configured with a die gap of 1.5–2.0 mm, a blow-up ratio of 1.8:1–2.5:1, and layer-specific melt temperatures between 210 °C and 240 °C, with each HDPE skin representing 20–35 wt% of the total structure. The HDPE skins crystallize faster than the barrier core after the frost line; if the frost line drops below 5 times the die diameter, the skins block in the collapsing frame and generate crescent-shaped wrinkles at the gusset. Food-contact compliance requires EU Regulation 10/2011 overall migration below 10 mg/dm², specific migration limits for slip and antiblock additives, and FDA 21 CFR 177.1520(c) for the olefin polymer. Terminal products are cereal box liners and dry food pouch stock.

    Carbon Black Dispersion and OIT Retention in HDPE Geomembrane Roll Goods

    Geomembrane sheet produced from HDPE TR144 is converted on flat-die cast film or thick blown-film lines, where thickness control and carbon black dispersion determine long-term oxidative resistance. The formulation uses 100 phr HDPE TR144, 2–3 phr carbon black masterbatch to achieve 2.0–2.5 wt% carbon black, 0.2–0.5 phr hindered phenol/phosphite antioxidant, and 0.1–0.2 phr HALS; fillers are excluded because additional inorganic loading above 3.5 phr carbon black reduces wedge-seam weld strength. Processing is carried out at melt temperatures of 205–225 °C, with die gaps between 2.0 mm and 3.0 mm, producing roll goods in thicknesses from 0.75 mm to 2.5 mm and widths up to 8 m on multi-roll stacking lines. Production-scale failures occur when carbon black masterbatch dispersion is poor: agglomerates larger than 100 µm are observed in transmitted light samples, oxidative induction time under ASTM D3895 drops below 100 min at 200 °C, and the sheet develops microcracks at seam folds during installation. Compliance for landfill and pond applications is governed by GRI-GM13, with density by ASTM D1505, tensile by ASTM D6693, and carbon black dispersion by ASTM D5596. Terminal products are landfill liners, pond and canal liners, and mining heap leach pad barriers.

    Multi-wall paper bag liners extruded from HDPE TR144 are typically produced as tubular film of 25–60 µm thickness using 100 phr resin with 500–1000 ppm slip and 1500–3000 ppm antiblock, at a die gap of 1.0–1.5 mm, a blow-up ratio of 2:1–3:1, and a melt temperature of 190–210 °C, for insertion into multi-wall paper sacks used in pet food, flour, and seed packaging under FDA 21 CFR 177.1520 and EU Regulation 10/2011.

    When Thin-Gauge Produce Bag Film Requires a Minimal Seal Initiation Temperature

    When HDPE TR144 is drawn down to 8–15 µm for produce bags on high-speed wicketing lines, the film must retain sufficient melt strength and antiblock performance without increasing the seal initiation temperature beyond the operating window of rotary sealing bars. The formulation is 100 phr HDPE TR144, erucamide or oleamide slip at 500–1200 ppm, synthetic silica antiblock at 1500–3000 ppm, and fluoroelastomer processing aid at 0.02–0.05 phr; inorganic filler is omitted to preserve tear resistance and visual clarity. The blown-film line operates with a die gap of 1.0–1.2 mm, a blow-up ratio of 3:1–4:1, high-stalk internal bubble cooling, and melt temperatures between 200 °C and 220 °C; the resulting film is gusseted, perforated, and fed to wicketing machines at 250–350 bags/min. Below 10 µm, static charge accumulation on the collapsing frame produces sticking and misalignment on the wicketing wicket; if antistatic additive is added at 0.1–0.3 phr, it must be tested for migration interaction with the slip package to avoid blocking. Food-contact compliance follows FDA 21 CFR 177.1520(c) and EU Regulation 10/2011, while tensile and tear properties are verified by ISO 527-3 and ISO 6383-2. Terminal products are produce bags, bakery bags, and ice bags.

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    Certification & Compliance
    More Introduction

    Shandong Yulong HDPE TR144 is a high-density polyethylene extrusion resin supplied for pressure piping systems in which long-term hydrostatic strength and slow crack growth resistance are the controlling design parameters. The designation TR144 identifies a bimodal molecular weight architecture; when the grade is certified as PE100, the compound carries a minimum required strength of 10 MPa at 20°C for 50 years under ISO 12162. The supplier’s technical datasheet is the governing source for batch-specific values, but the class-typical envelope includes a density of 0.950–0.960 g/cm³ at 23°C per ISO 1183-1 and a melt flow rate of 0.3–0.5 g/10 min at 190°C/5 kg per ISO 1133-1. The grade is used in potable water distribution, industrial process piping, and gas distribution where the applicable system standards are ISO 4427, EN 12201, and ISO 4437.

    What Distinguishes the Bimodal Molecular Architecture of TR144 From Unimodal PE80 Resins?

    The primary structural distinction is the bimodal molecular weight distribution. A low-molecular-weight fraction supplies shear thinning during extrusion, while a high-molecular-weight fraction provides tie-molecule density across the crystalline lamellae. Unimodal PE80 resins cannot separate these functions as effectively: raising the average molecular weight to improve stress crack resistance also elevates melt viscosity and reduces output. The high-molecular-weight tail of TR144 is designed to increase the strain hardening modulus measured at 80°C according to ISO 18488; strain hardening modulus values above 70 MPa are commonly associated with acceptable slow crack growth performance in PE100 pipe compounds. The same molecular architecture increases survival time in the notched pipe test under ISO 13479 at 80°C and 4.0 MPa, where PE100-class materials are generally required to resist brittle failure for at least 500 h. The different slow crack growth response is the main reason TR144 is specified in pressure piping instead of conventional blow-moulding or film-grade HDPE resins.

    Comonomer type and short-chain branch distribution influence slow crack growth more than melt index alone. Pipe-grade PE100 compounds typically use 1-butene or 1-hexene as comonomer. A 1-hexene–modified resin generally produces a higher tie-molecule density at equal density and crystallinity, which can improve slow crack growth resistance. Shandong Yulong HDPE TR144 should be accompanied by a datasheet that states the comonomer type and the density measured by ISO 1183-1; independent published data for this specific configuration is limited. Density should not be used as the sole predictor of pipe performance. Tensile creep rupture data generated under ISO 9080 are required to establish the hydrostatic design basis and to confirm that the grade meets the 10 MPa minimum required strength at 20°C for 50 years.

    Mechanical property data for PE100 pipe compounds of the TR144 class include tensile yield strength of 22–25 MPa and elongation at break greater than 600% when tested according to ISO 527-2 at 23°C and 50 mm/min. Flexural modulus is typically 800–1000 MPa, but these values vary with pipe wall crystallinity and conditioning. The notched Charpy impact strength at 23°C is generally above 20 kJ/m², but low-temperature impact behavior should be confirmed because it depends on comonomer type and molecular weight distribution. These mechanical properties support handling and installation loads but are secondary to the hydrostatic design basis for pressure rating.

    Rheological Response and Extrusion Limits in Grooved-Barrel Pipe Lines

    Processing of bimodal PE100 pipe compounds on production-scale single-screw extruders with grooved feed sections and L/D ratios of 30:1 to 33:1 requires a controlled barrel profile, usually from 180°C in the feed zone to 210–220°C at the metering zone. Melt temperature should be maintained between 190°C and 220°C. The die head is normally set 5–10°C above the adapter temperature to suppress melt fracture. Processing above 240°C is not recommended because extended residence time at that temperature accelerates oxidative degradation, leading to gel formation and black specks in the pipe wall. Shandong Yulong HDPE TR144 does not require pre-drying when the packaging is intact and warehouse relative humidity is below 60%. If surface condensation is observed, a hopper dryer at 70–80°C for 2–3 h is sufficient. Melt pressure before the screen pack is a critical process variable; on extruders with screw diameters of 25–40 mm, pressures of 15–30 MPa are common, but actual values depend on die resistance and screen condition.

    Output limits are governed by melt strength and the onset of sharkskin melt fracture, not only by screw plasticating capacity. The high-molecular-weight fraction increases extensional viscosity and die swell, so die land geometry and temperature must be adjusted during start-up. Production experience on 63 mm and 110 mm pipe lines indicates that die head pressures above 25 MPa at the screen changer can destabilize grooved-feed intake, causing throughput oscillation. Published data for Shandong Yulong HDPE TR144 in this specific configuration is limited; therefore, initial trials should map melt pressure, screw speed, haul-off speed, and pipe surface quality before fixed production settings are released.

    When Hydrostatic Design Basis and Slow Crack Growth Data Are Audited

    For pressure pipe certification, the hydrostatic design basis is established by long-term pressure testing of pipe specimens according to ISO 9080. A PE100 classification requires that the lower confidence limit of the long-term hydrostatic strength at 20°C for 50 years is not less than 10 MPa. Shandong Yulong HDPE TR144, when supplied as a PE100 pressure pipe compound, should meet this minimum required strength and is used with a design stress of 8 MPa for water at 20°C under the 1.25 service factor of ISO 4427. Slow crack growth is assessed by the notched pipe test according to ISO 13479; the usual acceptance criterion for PE100 pipe compounds is no brittle failure before 500 h at 80°C and 4.0 MPa. Rapid crack propagation is evaluated by the S4 test under ISO 13477, and PE100 materials are commonly specified with a critical temperature of -10°C or lower. For gas distribution, the design stress is also 8 MPa at 20°C under ISO 4437.

    For a PE100 pipe, the maximum operating pressure is calculated from the design stress and standard dimension ratio. At 20°C, a design stress of 8 MPa yields a pressure rating of 16 bar for SDR 11, 12.5 bar for SDR 13.6, and 10 bar for SDR 17 according to ISO 4427-2. The same SDR series applies to gas pipes under ISO 4437 with derating factors for higher temperatures. The pipe manufacturer must confirm these ratings after wall-thickness and tolerance verification, because resin MRS alone does not guarantee the final product rating.

    Comparative property envelope for PE100-class bimodal HDPE pipe compound and PE80 unimodal HDPE
    PropertyTest methodPE100 bimodal classPE80 unimodal class
    Minimum required strength at 20°C, 50 yearsISO 9080 / ISO 1216210 MPa8 MPa
    Density at 23°CISO 1183-10.950–0.960 g/cm³0.940–0.955 g/cm³
    Melt flow rate at 190°C/5 kgISO 1133-10.3–0.5 g/10 min0.4–0.8 g/10 min
    Oxidation induction time at 200°CEN 728≥20 min≥20 min
    Carbon black content for black pipeISO 69642.0–2.5 wt%2.0–2.5 wt%
    Notched pipe test at 80°C/4.0 MPaISO 13479≥500 h100–500 h

    Compared with unimodal PE80, the PE100 structure of TR144 permits a thinner wall at equal pressure rating because the design stress is 8 MPa rather than 6.3 MPa. This reduces mass per meter and increases internal diameter, but it also requires tighter control of wall-thickness eccentricity and residual stress. Compared with other PE100 grades, the differentiation of TR144 may arise from its molecular weight distribution, comonomer type, carbon black masterbatch, and stabilizer package. If the grade is a black compound with carbon black content of 2.0–2.5 wt% per ISO 6964, it is intended for outdoor storage and direct burial without additional UV masterbatch. Natural or colored variants require separate weathering stabilization. Mixing TR144 with PE80 scrap in the certified pressure pipe layer is not permitted under ISO 4427 or EN 12201 because the lower-strength component would reduce the long-term hydrostatic strength. In non-pressure drainage pipe, such mixing may be acceptable if the pipe is not certified as a pressure pipe and the final product is evaluated for impact and stiffness separately.

    Although the grade is optimized for pressure pipe, it may also be evaluated for non-pressure applications such as large-diameter spiral-wound drainage pipe, manhole liners, and industrial ducting. In these applications, ring stiffness, creep modulus, and impact strength control design rather than hydrostatic strength. The same welding and extrusion limits apply, but the elevated MRS of PE100 is not fully utilized. If the grade replaces a lower-density unimodal HDPE in such products, the higher density increases ring stiffness but may reduce impact toughness at low temperatures; the final product should be tested to the relevant ISO or ASTM impact method.

    Compliance checklist matrix for pressure pipe applications
    RequirementStandard/test methodTypical acceptance criterion
    DensityISO 1183-10.950–0.960 g/cm³ at 23°C
    Melt flow rateISO 1133-10.3–0.5 g/10 min at 190°C/5 kg
    Carbon black contentISO 69642.0–2.5 wt%
    Carbon black dispersionISO 18553≤ grade 3
    Oxidation induction timeEN 728≥20 min at 200°C
    Hydrostatic strengthISO 9080 / ISO 12162MRS 10 MPa
    Notched pipe testISO 13479≥500 h at 80°C/4.0 MPa
    Rapid crack propagation S4ISO 13477critical temperature ≤ -10°C

    The stabilizer system is a critical difference between pipe grades that otherwise share similar density and melt flow rate. Pipe-grade PE100 compounds require long-term thermal-oxidative stability under wet and dry conditions. For potable water service, the formulation must comply with the applicable positive list and migration limits; for gas service, the stabilizer should not introduce extractable compounds that interfere with odorant retention or inner surface quality. Oxidation induction time measured by EN 728 at 200°C is commonly specified as ≥20 min, but OIT is a quality-control indicator and does not directly predict 50-year pipe life. The grade is not recommended for continuous exposure to strong oxidizing acids, aromatic hydrocarbons, or chlorinated solvents at elevated temperature. In chlorinated water distribution, the pipe producer must verify the specific chlorinated-water resistance of Shandong Yulong HDPE TR144 under the relevant test protocol, such as ASTM F2263; published data for this specific configuration is limited.

    Fusion compatibility with PE100 fitting grades is required for butt welding and electrofusion. Melt flow rate mismatch greater than 0.5 g/10 min between pipe and fitting can reduce weld strength; therefore, the pipe and fitting should be matched according to the fitting manufacturer’s approved resin list. Thermal stability at welding temperatures of 220–230°C should be verified by melt flow shift less than ±20% after a 30 min thermal exposure if required by the utility specification.

    Carbon black dispersion is another quality criterion for black pipe. ISO 18553 requires a dispersion rating of grade 3 or better to prevent local stress concentrations that can initiate slow crack growth. Poor dispersion can be detected by microtome observations and should trigger review of masterbatch letdown ratio and screw mixing. For Shandong Yulong HDPE TR144 black grades, the producer should verify dispersion on the finished pipe wall, not only on the pellet.

    On manufacturing lines, the most common defect associated with bimodal PE100 pipe extrusion is gel formation from unmelted high-molecular-weight particles. This is observed as surface protrusions or inner-wall roughness and is minimized by barrier screws with adequate mixing sections and by progressive screen packs. Melt temperature stratification in the adapter can also produce localized degradation. Ultrasonic wall-thickness scanning may reveal periodic thickness variation linked to melt pressure oscillation or screw speed pulsation. A melt pump can reduce short-term wall-thickness variation, but the calibration sleeve vacuum and cooling tank alignment must be stable to maintain roundness. These processing considerations are not unique to TR144, but the high-molecular-weight fraction makes the grade less forgiving of low shear heating and improper screw geometry than lower-viscosity PE80 or unimodal HDPE.

    Storage and handling of Shandong Yulong HDPE TR144 should prevent prolonged exposure to direct sunlight and storage temperatures above 40°C to avoid stabilizer migration and pellet blocking. Bags or octabins should be kept closed when not in use. Batch release documentation should be audited for density, melt flow rate, tensile yield strength, elongation at break, and stabilizer content. If the material is to be used in potable water service, the final pipe must be tested against the applicable national certification scheme, not only against the resin datasheet.

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