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TPC (Japan) HDPE KL372A

    • Product Name: TPC (Japan) HDPE KL372A
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 589569
    Density 0.954 g/cm3
    Melt Flow Rate 190 C 2 16 Kg 0.30 g/10 min
    Tensile Strength At Yield 25.0 MPa
    Tensile Strength At Break 30.0 MPa
    Elongation At Break 800 %
    Flexural Modulus 1.10 GPa
    Izod Impact Strength Notched 0.200 J/cm
    Shore D Hardness 66
    Vicat Softening Point 125 C
    Melting Point 133 C
    Brittleness Temperature -70.0 C
    Environmental Stress Crack Resistance >1000 hr
    Thermal Conductivity 0.44 W/m-K
    Coefficient Of Linear Thermal Expansion 1.2E-4 1/C
    Specific Heat Capacity 1.9 J/g-C
    Dielectric Constant 2.3
    Dissipation Factor 0.0002
    Volume Resistivity >1.0E15 ohm-cm
    Dielectric Strength 20 kV/mm

    As an accredited TPC (Japan) HDPE KL372A factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing TPC (Japan) HDPE KL372A is supplied in 25 kg multiwall paper sacks, palletized and stretch-wrapped for secure industrial delivery.
    Container Loading (20′ FCL) Standard Container Loading (20′ FCL) for TPC (Japan) HDPE KL372A: palletized 25 kg bags, shrink-wrapped, securely stowed for export.
    Shipping TPC (Japan) HDPE KL372A is a non-hazardous polyethylene resin, typically supplied in 25 kg bags or jumbo bags, palletized and stretch-wrapped. Ship in clean, dry containers or trucks at ambient temperature, avoiding moisture, direct sunlight, and excessive heat. Follow supplier SDS and local transport regulations.
    Storage Store TPC (Japan) HDPE KL372A in a cool, dry, well-ventilated warehouse. Keep away from direct sunlight, heat, flames, ignition sources, and strong oxidizers. Maintain sealed original bags or containers, stack on pallets off the floor, and prevent moisture, dust, and contamination. Avoid prolonged UV exposure. Follow local regulations and use first-in, first-out rotation. Inspect packaging regularly.
    Shelf Life TPC (Japan) HDPE KL372A typically has indefinite shelf life when stored dry, unopened, away from heat, sunlight, and contamination.
    Application of TPC (Japan) HDPE KL372A

    A 220 L tight-head blow-moulded drum body produced from TPC HDPE KL372A relies on a nominal density of 0.954 g/cm³ (ASTM D1505-20) and a melt flow rate of 0.07 g/10 min (ASTM D1238-20, 190 °C/2.16 kg) to maintain parison sag resistance at melt temperatures of 190–210 °C on accumulator-head extrusion blow-moulding machines with screw L/D ratios between 24:1 and 30:1. In this downstream production process, the high-molecular-weight fraction permits a programmed parison wall thickness of 3.5–5.0 mm in the body section, while the mould is held at 10–30 °C and inflated at 0.6–0.8 MPa; cooling time is typically 180–300 s before flash removal and automatic leak testing. The formulation addition ratio for UN-certified service allows clean internal regrind reincorporation at ≤30 wt% of the total shot weight, and carbon black masterbatch is metered at 2.0–2.5 wt% when opacity or outdoor weathering is specified; higher regrind levels require re-validation of drop impact and hydrostatic burst performance because the low-melt-flow base resin responds to regrind-induced viscosity reduction with measurable parison drawdown variation. Industry compliance is governed by UN Model Regulations Chapter 6.1 for plastics drums coded 1H1/Y1.8/250, requiring a hydrostatic pressure test at 250 kPa for 30 min, a 1.2 m drop test after conditioning at −18 °C, and a stack-load test at 40 °C for 28 days; material ESCR is verified under ASTM D1693-21 Condition B, 100 % Igepal, with values exceeding 1,000 h. The terminal finished product type is the UN-certified 220 L L-ring tight-head polyethylene drum used for liquid hazardous chemicals, fitted with 2 in and 3/4 in bungs and sealed with tamper-evident closures.

    In closed-loop extrusion blow-moulding of 1,000 L composite intermediate bulk container inner bottles, TPC HDPE KL372A is processed at a melt temperature of 190–210 °C through an accumulator head with parison length control accommodating preform lengths of 1.5–1.8 m; the mould clamp unit is typically rated between 1,000 kN and 1,500 kN to maintain parting-line integrity during inflation at 0.6–0.8 MPa. The downstream production process uses a single-layer parison with programmed wall thickness distribution optimized for corner thinning, because the inner bottle must resist stack loads and hydraulic pressure without metallic overpack reinforcement. The formulation addition ratio allows clean internal regrind at ≤35 wt% of the total charge, while UV-stabilized masterbatch is dosed at 1.5–2.0 wt% when the composite IBC is intended for outdoor storage; any regrind source contaminated with hydrocarbon solvents or amines is excluded to avoid stress-cracking initiation in the discharge valve seat and sidewall bend zones. Industry compliance is evaluated under UN Model Regulations Chapter 6.5 for rigid plastics composite IBCs coded 31HA1/Y, with bottom drop tests from 1.2 m at −18 °C, top-lift and stack-load tests per the applicable UN test sequence, and dimensional verification of the inner receptacle interface before assembly into the steel cage. The terminal finished product type is the UN-certified 1,000 L composite IBC inner bottle, with an integrally moulded 150 mm top fill neck and a lower discharge valve seat compatible with 2 in butterfly or ball valve assemblies.

    What Limits Regrind Reincorporation in Six-Layer Automotive Fuel Tank Coextrusion?

    Six-layer fuel tank coextrusion places the highest demand on HDPE KL372A because the substrate skins must carry the parison during blow moulding while the EVOH barrier and tie layers remain continuous at total thicknesses below 10 mm. The process is run on a multi-layer accumulator-head blow-moulding machine with six extruders, melt temperatures of 210–230 °C for the HDPE skins and 200–220 °C for the tie and barrier layers, an annular die gap of 1.5–3.0 mm, and a mould close speed of 200–400 mm/s to limit fold-over defects at pinch-off seams. The formulation addition ratio positions TPC HDPE KL372A as the outer and inner skins at 70–80 wt% of the total tank mass; ethylene-vinyl alcohol copolymer is introduced at 1.5–3.0 wt%, maleic anhydride-grafted polyethylene tie layers at 2–3 wt% per layer, and clean plant regrind from the same six-layer scrap at 20–30 wt% of the HDPE fraction. Regrind content above 30 wt% produces measurable increases in parison sag and barrier layer thickness variation, which translates into elevated hydrocarbon permeation values on finished tanks. Industry compliance standards include UN ECE R34 Annex 5 for fire resistance and post-impact fuel leakage, hydrocarbon evaporative emission limits under EPA Tier 3 and CARB LEV III, SAE J2587 for permeation evaluation, and material-level tensile and ESCR testing under ASTM D638-14 and ASTM D1693-21 Condition B. The terminal finished product type is the automotive fuel tank for gasoline and oxygenated blends up to E10, with a six-layer wall structure and a nominal shell thickness of 6–10 mm depending on vehicle package space.

    Layer sequenceMaterialWeight fractionGoverning standard
    Outer skinTPC HDPE KL372A35–40 wt% of tank massASTM D1693-21
    Tie layerMaleic anhydride-grafted polyethylene2–3 wt% per layerSAE J2587
    Barrier layerEthylene-vinyl alcohol copolymer1.5–3.0 wt%ASTM D3985-17
    Tie layerMaleic anhydride-grafted polyethylene2–3 wt% per layerSAE J2587
    Inner skinTPC HDPE KL372A35–40 wt% of tank massASTM D1693-21
    Regrind fractionClean six-layer fuel tank scrap20–30 wt% of HDPE fractionASTM D1238-20

    When Carbon Black Masterbatch Extends UV Resistance in Moored Buoy Shells

    Outdoor moored buoy shells produced from TPC HDPE KL372A require compounded UV stabilization because the part must retain notched impact strength after multi-year exposure to saltwater, cyclic wave loading, and solar radiation. The downstream process is extrusion blow moulding on a twin-station accumulator-head machine with a melt temperature of 190–210 °C, a mould temperature of 10–30 °C, and a parison programming sequence that increases wall thickness to 8–15 mm at the top mooring eye and lower skirt attachment points. The formulation addition ratio for UV-stabilized buoy shells specifies a polyethylene-carrier carbon black masterbatch at 2.0–2.5 wt% to achieve a final carbon black content near 2.0 wt%, and a hindered amine light stabilizer masterbatch at 0.2–0.5 wt% when extended weathering resistance is specified; the masterbatch carrier is matched to high-molecular-weight HDPE to avoid melt-viscosity inversion during blending. Industry compliance for such components is not governed by a single mandatory global standard, so qualification is typically anchored to ASTM G154 Cycle 1 or ISO 4892-3 accelerated weathering, ASTM D638-14 tensile properties after 2,000–5,000 h exposure, and ASTM D1693-21 Condition B ESCR after environmental stress-cracking exposure; published data for this specific configuration is limited, and end users typically require Xenon arc or Florida outdoor exposure validation before acceptance. The terminal finished product type is the blow-moulded double-walled shell for moored navigation buoys, marker floats, and fender floats, filled with closed-cell polyurethane foam after moulding to prevent water ingress and maintain buoyancy after shell puncture.

    Blow-moulded selective catalytic reduction urea tanks manufactured from TPC HDPE KL372A are produced by monolayer extrusion blow moulding or by coextruding a carbon black outer skin over a natural or black inner layer, with melt temperatures of 190–210 °C, mould temperatures of 10–30 °C, and programmed parison wall thicknesses of 3–6 mm to support ultrasonic welding bosses and heating element brackets. The formulation addition ratio restricts non-contaminated plant regrind to ≤20 wt% of the total shot weight because higher levels reduce environmental stress-cracking resistance after prolonged exposure to 32.5 wt% aqueous urea solution; carbon black masterbatch is dosed at 2.0–2.5 wt% for opacity and UV resistance, while amine-based processing aids are excluded due to the risk of extractable nitrogen species migrating into the fluid. Industry compliance is evaluated under ISO 22241-1:2019 for diesel exhaust fluid AUS 32 quality and ISO 22241-3:2017 for materials compatibility and storage, with long-term immersion testing in AUS 32 at 60 °C for 3,000 h used to screen resin suitability; published data for this specific KL372A configuration is limited, so formal qualification against the vehicle manufacturer's material specification is required. The terminal finished product type is the SCR urea solution tank for heavy-duty diesel and off-road aftertreatment systems, fitted with a 50–100 mm filler neck, level sensor port, and heated suction line boss.

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