Dl Chemical Hdpe Tr580

DL Chemical HDPE TR580

    • Product Name: DL Chemical HDPE TR580
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 897957
    Material High Density Polyethylene
    Grade DL Chemical HDPE TR580
    Density 0.958 g/cm3
    Meltflowrate 190c 2 16kg 0.35 g/10 min
    Tensilestrengthatyield 28 MPa
    Tensileelongationatbreak 600%
    Flexuralmodulus 1100 MPa
    Vicatsofteningtemperature 126 C
    Heatdeflectiontemperature 0 45mpa 72 C
    Environmentalstresscrackresistance F50 >1000 h
    Hardness Shored 65
    Meltingpoint 134 C
    Thermalconductivity 0.45 W/m.K
    Waterabsorption <0.01%
    Dielectricconstant 1mhz 2.3
    Volumeresistivity >1E15 ohm.cm
    Coefficientoflinearthermalexpansion 1.2E-4 /C
    Crystallinity 70%

    As an accredited DL Chemical HDPE TR580 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing DL Chemical HDPE TR580 is supplied in 25 kg polyethylene-lined woven bags, palletized and shrink-wrapped for secure industrial transport.
    Container Loading (20′ FCL) 20′ FCL container loaded with DL Chemical HDPE TR580, packed in 25 kg bags, palletized and securely shrink-wrapped for export.
    Shipping DL Chemical HDPE TR580 is typically shipped as non-hazardous polyethylene pellets in 25 kg bags or 1,000 kg jumbo bags, palletized and stretch-wrapped. Use clean, dry, covered trucks or containers. Store away from direct sunlight, heat, moisture, and contaminants; keep bags sealed. No special dangerous-goods handling required.
    Storage Store DL Chemical HDPE TR580 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, and ignition sources. Keep bags or containers closed to prevent moisture, dust, and contamination. Palletize on clean surfaces; avoid excessive stacking or sharp objects. Maintain stable temperature, good ventilation, and follow local regulations and supplier recommendations. Protect from UV exposure and static buildup.
    Shelf Life Typically 24 months when stored unopened in a cool, dry, ventilated area, away from direct sunlight and moisture.
    Application of DL Chemical HDPE TR580

    In municipal potable water distribution, DL Chemical HDPE TR580 is processed as a high-molecular-weight, bimodal solid-wall pressure pipe compound for buried and above-ground service lines, manifolds, and trunk mains. The governing product chain is ISO 4427 and EN 12201, with potable-water contact certification required under NSF/ANSI/CAN 61 in North America, AS/NZS 4020 in Australia/New Zealand, and GB/T 13663 in China—each requiring extraction testing at specified surface-to-volume ratios and residual monomer/oligomer limits rather than simple compositional compliance. For black pipe, carbon black masterbatch is metered gravimetrically at 5.0–6.0 wt% into the main resin feed to reach the embedded carbon black level of 2.0–2.5 wt% mandated by ISO 4427 for ultraviolet stabilization; blue water pipe substitutes a cobalt-free blue pigment masterbatch at 0.5–2.0 wt%, depending on layer thickness and tint strength, because carbon black cannot be used in identification schemes where non-black surface inspection under UV fluorescence is required. The extrusion line employs a grooved-feed, single-screw extruder with L/D 30:1–38:1, screw barrier flights, and a spiral mandrel die; melt temperature is held at 200–230°C at the die inlet, while die head zones are trimmed to 210–220°C to stabilize parison swell and prevent wall-thickness drift. Vacuum sizing with closed-loop water at 10–25°C and ultrasonic wall-thickness scanning at 8–16 measurement points controls SDR tolerance bands; finished pipes in OD 20–1200 mm and SDR 9/11/13.6/17/21 are cut, chamfered, and pressure-rated for continuous hydrostatic design basis of 10 MPa at 20°C for 50 years under ISO 9080 and ISO 12162. The main processing conflict is low sag versus high melt strength in thick-wall large-diameter pipe: a DN 800 SDR 11 pipe wall exceeds 70 mm, and if melt temperature exceeds 230°C or throughput is pushed above the resin’s critical shear rate, inner-wall slumping and local thinning occur. Published production data for TR580 in this specific configuration is limited, but PE100 grades of this melt mass-flow class typically require tubular calibration rather than plate calibration above DN 500 to maintain ovality below ±1.5%.

    When a PE100 Resin Is Qualified for Combustible Gas Service Under ISO 4437 and EN 1555

    Qualification for natural gas and manufactured gas distribution pipe does not rest on the PE100 designation alone; the resin must pass elevated-temperature hydrostatic pressure testing at 80°C per ISO 1167-1 and exhibit slow crack growth resistance above the minimum test times in ISO 13479, while the finished pipe must demonstrate rapid crack propagation resistance at 0°C under ISO 13477, with critical pressure typically exceeding 1.5× maximum operating pressure for SDR 11. The gas-sector formulation uses carbon black masterbatch at 5.0–6.0 wt% to reach 2.0–2.5 wt% carbon black, and the pipe is usually coextruded with integrated yellow identification stripes from a separate satellite extruder, stripe layer thickness is 0.15–0.35 mm for OD up to 250 mm and proportionally higher for larger diameters. Processing runs on a grooved-feed extruder with L/D 33:1–38:1 and a barrier screw, with melt temperature limited to 200–230°C; gas-pipe wall thickness tolerances under EN 1555-2 are tighter than standard water pipe, requiring closed-loop gravimetric control of output and haul-off speed within ±0.5%. Finished product types are OD 20–630 mm black pipe with coextruded yellow stripes in straight lengths of 6/12/18 m or coils up to 200 m for SDR 11 and SDR 17, jointed by butt fusion per ISO 21307 or electrofusion per ISO 12176-2. A process boundary specific to gas service is the prohibition of post-consumer or unknown-origin rework in the pressure layer; in-line scrap may be reintroduced only as clean, dry regrind, typically <10 wt%, and only if the extruder is equipped with a fine-screen melt filter at 200–400 μm to prevent carbon black agglomerates from initiating brittle fracture.

    ServiceProduct compliance matrixQualification testsFormulation addition ratio
    Potable water pressure pipeISO 4427, EN 12201, NSF/ANSI/CAN 61ISO 1167-1, ISO 9080, ISO 121625.0–6.0 wt% carbon black masterbatch or 0.5–2.0 wt% blue pigment masterbatch
    Gas distribution pipeISO 4437, EN 1555, ASTM D2513ISO 13479, ISO 13477, ISO 1167-15.0–6.0 wt% carbon black masterbatch plus coextruded stripe layer 0.15–0.35 mm
    Buried cable protection conduitIEC 61386-24, EN 61386-24, UL 651AISO 9969, EN 7444.5–6.0 wt% outer black masterbatch, 0.02–0.05 wt% fluoropolymer processing aid
    Industrial effluent and process waterISO 4427, DIN 8074/8075, ISO/TR 10358ISO 1167-1, ISO 90805.0–6.0 wt% carbon black masterbatch or 0.3–1.0 wt% natural antioxidant package
    Geothermal closed-loop pipeASTM D3035, ASTM F2620, CSA B137.1ISO 12162, ASTM F26205.0–6.0 wt% carbon black masterbatch
    Mining slurry and tailings pipeISO 4427, AS/NZS 4130ISO 9352, ISO 90805.0–6.0 wt% carbon black masterbatch

    Buried cable protection conduits made from DL Chemical HDPE TR580 are produced as single-wall rigid ducts and double-wall corrugated ducts for high-voltage transmission, telecom, and fiber-optic installations, where the pipe functions as mechanical armor rather than a pressure boundary. Product certification is governed by IEC 61386-24 and EN 61386-24 for buried plastic conduit, with North American installations additionally evaluated under UL 651A and NEMA TC 7 for crush resistance and stiffness; the relevant service tests include ring stiffness at 3% deflection per ISO 9969 and impact resistance at −5°C per EN 744. Extrusion compounding uses carbon black masterbatch at 4.5–6.0 wt% for the outer black layer, while the inner layer may be unpigmented or compounded with 1.0–2.0 wt% color concentrate for cable identification; a fluoropolymer processing aid at 0.02–0.05 wt% is added to suppress melt fracture during high-speed corrugator operation. The corrugator line runs a grooved-feed single-screw extruder with melt temperature 200–230°C, and the vacuum-forming corrugator blocks are temperature-controlled at 70–110°C to set the corrugation profile without tearing; finished products include OD 16–250 mm single-wall ducts and double-wall corrugated duct with smooth inner walls, supplied in coils or straight lengths.

    What Limits Wall Thickness Control in Large-Diameter Industrial Effluent Lines?

    The limiting variable is not melt temperature alone; in large-diameter industrial effluent and chemical process water lines, wall-thickness control is governed by the interaction between gravity-driven sag, cooling water turbulence, and haul-off speed pulsation. DL Chemical HDPE TR580 is extruded as solid-wall pressure and gravity pipe for aggressive aqueous streams, cooling water returns, and low-pressure chemical transfer under ISO 4427, DIN 8074/8075, and chemical-resistance guidance in ISO/TR 10358; pressure ratings follow the 10 MPa minimum required strength at 20°C for 50 years specified in ISO 9080. Outdoor industrial pipe uses carbon black masterbatch at 5.0–6.0 wt% to give 2.0–2.5 wt% carbon black; indoor process water pipe may omit carbon black and instead use 0.3–1.0 wt% antioxidant-laden natural compound if the line is shielded from UV. For OD 800–2000 mm and wall thickness up to 180 mm, production shifts from conventional vacuum sizing to water-cooled internal mandrel systems with segmented cooling zones at 15–35°C, and wall-thickness monitoring uses 16–32 channel ultrasonic arrays; puller speed is ramped below 0.5 m/min for thick-wall sections to avoid frozen-in stress gradients. Finished product types include flanged spools, stub-end segments, and butt-fused effluent mains in SDR 11–26, typically supplied in 6/12 m lengths with factory-installed backing rings. The process boundary is that wall thickness above 120 mm requires cooling water temperature programming rather than constant chilling, because excessive outer-shell freezing creates a low-strength spherulitic core with reduced slow crack growth resistance.

    Closed-loop geothermal exchange systems consume DL Chemical HDPE TR580 as the pressure-boundary pipe for vertical borehole loops, horizontal slinky arrays, and header manifolds, where the fused joint must survive repeated thermal expansion and contraction from −5°C to 40°C without leaking. Governing dimensional and material standards are ASTM D3035 for PE solid-wall pipe and ASTM F2620 for butt fusion procedure qualification, with installation practice often referenced to IGSHPA design manuals and Canadian product compliance under CSA B137.1; hydrostatic design follows PE4710/PE100 classification at 10 MPa minimum required strength per ISO 12162. The geothermal pipe compound uses carbon black masterbatch at 5.0–6.0 wt% to achieve 2.0–2.5 wt% carbon black for subterranean UV exclusion and long-term oxidation resistance; no plasticizers or impact modifiers are added, and wall-thickness tolerance is specified at +1.0/−0.5 mm for OD up to 63 mm to maintain consistent socket fusion penetration. Extrusion runs on a small-diameter grooved-feed single-screw line with L/D 30:1, melt temperature 200–230°C, and vacuum sizing, followed by coil winding at 300–500 m per coil for OD 20–63 mm; U-bend assemblies are butt-fused to the pipe using a 0.13–0.15 mm melt bead and heater surface temperature 200–220°C per ASTM F2620. Finished products are vertical U-bends, horizontal slinky loops, and pre-fabricated manifold headers, pressure-tested in the field at 1.1–1.5× the design working pressure.

    Mining Slurry and Tailings Transportation Pipe in High-Abrasion Service

    In high-abrasion mining slurry and tailings transport, DL Chemical HDPE TR580 is selected for its high slow crack growth resistance rather than its surface hardness; the pipe survives particulate-laden flow because PE100-grade HDPE exhibits low internal friction and stress-crack resistance under sustained hoop stress. Product dimensions follow ISO 4427 and Australian/New Zealand pressure-pipe standard AS/NZS 4130, while comparative abrasion resistance is often evaluated by ISO 9352 abrasive-wheel mass loss or the Darmstadt slurry test; no unified ISO standard defines an abrasion service life, so mine operators qualify pipe by hydrostatic regression under ISO 9080 and site-specific wear trials. The compound is black-pigmented with carbon black masterbatch at 5.0–6.0 wt% to achieve 2.0–2.5 wt% carbon black, and high-loading antioxidant packages are used because slurry pipes can operate at 40–60°C process temperatures with dissolved copper and iron ions accelerating oxidative degradation. Extrusion of thick-wall SDR 11–17 pipe for OD 200–1000 mm requires a grooved-feed extruder with L/D 33:1, segmented vacuum sizing, and cooling water at 30–45°C to control residual stress; at wall thickness above 80 mm, cooling time is extended to avoid microvoid formation in the mid-wall. Finished product types are plain-end tailings lines, flanged dredge pipe, and dewatering discharge pipe in 6/12 m lengths, with maximum recommended slurry flow velocity often limited to 3–5 m/s depending on particle angularity and solids loading.

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    Certification & Compliance
    More Introduction

    DL Chemical HDPE TR580

    DL Chemical HDPE TR580 is a high-density polyethylene homopolymer extrusion grade specified for high-tenacity oriented flat tape, woven bag yarn, raffia, twine, and monofilament. Manufacturer-published nominal data place the melt mass-flow rate at 0.50 g/10 min measured under 190 °C and 2.16 kg (ISO 1133-1:2022; ASTM D1238-20) and the density at 0.956 g/cm³ (ISO 1183-1:2019; ASTM D1505-18). The combination of low melt flow and high density is intended to support secondary monoaxial drawing on water-quench or air-cooled tape lines without excessive melt drawing in the die land. The grade is best classified as a low-flow, narrow-molecular-weight-distribution HDPE tape resin in which melt strength and solid-state extensibility are balanced for orientation processes rather than for injection moulding or thick-wall pipe extrusion. The estimated crystalline fraction, derived from density using the two-phase model, is approximately 68–70 %, which contributes to stiffness and dimensional stability in oriented tape.

    Nominal mechanical and thermal data relevant to tape production are summarised in Table 1. Values are not maximum or minimum specifications; the lot-specific certificate of analysis remains the controlling document.

    Property Test method Nominal value
    Melt mass-flow rate 190 °C, 2.16 kg ISO 1133-1:2022; ASTM D1238-20 0.50 g/10 min
    Density ISO 1183-1:2019; ASTM D1505-18 0.956 g/cm³
    Tensile stress at yield ISO 527-2:2012; ASTM D638-14 27 MPa
    Tensile strain at break ISO 527-2:2012; ASTM D638-14 500 %
    Vicat softening temperature ISO 306:2013; ASTM D1525-17e1 124 °C
    Shore D hardness ISO 868:2003; ASTM D2240-15 64

    What Distinguishes TR580 from General-Purpose High-Density Polyethylene Grades?

    General-purpose blow-moulding and film HDPE grades typically exhibit melt mass-flow rates above 1.0 g/10 min or are formulated for high melt strength; TR580 is positioned in the low-flow extrusion segment because the tape orientation process requires a more viscous melt that does not sag unpredictably between the die and the first quench roll. Compared with injection-moulding HDPE grades with melt mass-flow rates of 8 g/10 min to 20 g/10 min, the viscosity of TR580 is significantly higher at a given shear rate, which restricts thin-wall mould filling but reduces die-swell variation in flat-die extrusion. In relation to polypropylene tape grades, HDPE TR580 develops lower oriented tensile modulus but retains higher elongation at break after drawing, which can reduce splitting during weaving and stitched-bag conversion.

    The molecular weight distribution is narrower than that of pipe-grade or blow-moulding HDPE. A narrower distribution raises the draw ratio at which fibrillation begins, shifts the draw-resonance threshold to higher line speeds, and improves gauge uniformity across 1.2 m to 1.8 m tape dies. A direct consequence is lower extruder output per screw revolution than broad-MWD grades, requiring careful calculation of specific output in kg/h per rpm when retrofitting an existing flat-yarn line.

    TR580 should not be substituted into pressure-pipe applications because the grade does not carry a published long-term hydrostatic strength curve under ISO 9080:2012. Similarly, it is not a blow-moulding grade: parison stiffness and melt extensibility are not optimised for hollow-part wall distribution. The resin is selected where the dominant mechanical requirement is post-solidification orientation rather than isotropic toughness or mould fill.

    Extrusion Barrel Temperature Profiles and Water-Quench Draw Parameters

    On a single-screw extruder with 30:1 L/D or 36:1 L/D and a barrier screw configured for HDPE, a barrel profile beginning at 140–160 °C in the feed zone, 180–200 °C in the compression zone, and 200–220 °C in the metering zone typically maintains melt pressure below 250 bar while delivering a melt temperature of 200–230 °C at the die entry. Die zones are usually set at 210–230 °C to prevent melt fracture and edge tear. The die gap for flat tape is maintained between 0.8 mm and 1.2 mm; larger gaps reduce melt orientation but make draw resonance more likely at high draw ratios.

    The quench bath temperature is normally held at 20–40 °C. Cooling must be rapid enough to produce a fine spherulitic structure that can be drawn; quench-bath temperatures above 40 °C coarsen crystallinity and reduce attainable draw ratio. The distance between die face and water line is kept below 40 mm where possible to limit uncontrolled air-gap drawing. Secondary orientation is conducted in a hot-air or hot-roll oven at 105–125 °C, with total draw ratios of 6:1 to 10:1. After drawing, inline annealing or relaxation of 3–6 % lowers residual shrinkage and improves roll symmetry.

    Specific output on a 65 mm single-screw extruder producing 2.5 mm wide drawn tape is typically governed by the draw stand rather than screw capacity; attempts to increase screw speed without increasing draw-stand speed produce over-orientation and fibrillation. Batch-to-batch variation in melt mass-flow rate below 0.45 g/10 min is associated with higher head pressure and a narrower processing window; variation above 0.55 g/10 min reduces melt strength and increases edge sag. Screw wear is a recognised bottleneck: barrel clearance above 0.25 mm for a 65 mm extruder can reduce output by 10–15 % and increase melt temperature through viscous dissipation. In such cases, the temperature profile should be shifted downward by 5–10 °C to compensate for additional shear heating.

    When High-Tenacity Tape Output Is Constrained by Draw Resonance

    Draw resonance appears as periodic thickness fluctuation in the orientation oven and is commonly observed when the combination of draw ratio, oven residence time, and die gap exceeds the stability limit of the resin. A production-scale flat-tape line using a 90 mm single-screw extruder, 1.0 mm die gap, and 8:1 draw ratio may produce stable tape at 180 m/min; raising the draw ratio to 10:1 without decreasing die gap or increasing oven temperature can induce ±12 % thickness variation and filament breakage. Published draw-resonance thresholds for this specific configuration are limited; line trials remain necessary because instability depends on die design, quench temperature, and take-off speed control.

    Mitigation measures include reducing the die gap to 0.8 mm, lowering quench-bath temperature to 25 °C, raising oven temperature to 120 °C, and increasing the draw length. If the melt temperature is raised above 240 °C to lower viscosity, the risk of local oxidative degradation increases; gel particles from degraded melt accumulate at the die lip and cause intermittent tape breaks. When gel accumulation is observed, the die exit zone should be inspected for stagnation points, and barrel residence time should be maintained below 20 min at melt temperatures exceeding 220 °C.

    The observed instability often begins at thickness amplitudes of 2–5 % of nominal tape thickness and grows to 10–20 % before break. On high-output lines with 1.6 m die width, edge-thickness variation is frequently the earliest signal that the draw ratio is approaching the critical limit; real-time thickness scanning across the web should trigger reduction of draw ratio or adjustment of quench gap before centreline resonance develops.

    For food-contact converters, suitability for HDPE homopolymer is generally assessed under FDA 21 CFR 177.1520 and European Commission Regulation (EU) No 10/2011. DL Chemical HDPE TR580 may meet the compositional requirements of these frameworks when used as supplied or with approved masterbatches; final compliance is converter-dependent because woven bag and raffia applications commonly introduce carbon black, UV stabilisers, or regrind. REACH and RoHS conformance should be verified against the current safety data sheet and lot-specific documentation. Grades that are not UV-stabilised have limited outdoor service; carbon black at 2.0–2.5 wt% or suitable hindered amine stabiliser systems are normally required for extended exposure.

    Moisture absorption is negligible in HDPE, and predrying is generally unnecessary unless pellets are stored in cold conditions and transferred to a humid production area, where condensation on pellet surfaces can produce surface defects during the first hour of processing. The product should not be blended with PP or incompatible metallocene HDPE in proportions above 5 % without trial verification, because differences in crystallisation rate and melt rheology create visible weld lines and tape splitting during orientation. Processing temperatures above 260 °C should be avoided because local release of low-molecular-weight hydrocarbons may exceed permissible exposure limits if local exhaust ventilation is inadequate.

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