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TPC (Japan) HDPE KS178A

    • Product Name: TPC (Japan) HDPE KS178A
    • 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 197358
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.956 g/cm³
    Melt Mass Flow Rate 190 C 2 16 Kg 8.0 g/10 min
    Melting Point 134 °C
    Vicat Softening Temperature 126 °C
    Tensile Strength At Yield 29 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break 1000 %
    Flexural Modulus 1180 MPa
    Notched Izod Impact Strength 40 J/m
    Shore D Hardness 65
    Mold Shrinkage 1.5-3.0 %
    Water Absorption <0.01 %
    Thermal Conductivity 0.44 W/m·K
    Volume Resistivity >1E16 ohm·cm

    As an accredited TPC (Japan) HDPE KS178A factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing TPC (Japan) HDPE KS178A is supplied in 25 kg polyethylene-lined paper bags, with 1,000 kg jumbo bags available.
    Container Loading (20′ FCL) 20′ FCL loading: TPC Japan HDPE KS178A in 25 kg bags, palletized, shrink-wrapped, approximately 17–18 MT net per container.
    Shipping TPC (Japan) HDPE KS178A is a non-hazardous high-density polyethylene resin. It is not regulated for transport under DOT, IMDG, IATA, or ADR. Ship in original sealed 25 kg bags, palletized and shrink-wrapped. Keep dry, avoid heat, contamination, and oxidizers. No special labels or placards required; not a marine pollutant.
    Storage Store TPC (Japan) HDPE KS178A in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags or containers closed, labeled, and off the floor on pallets. Prevent moisture, dust, and contamination. Avoid prolonged UV exposure and excessive stacking. Rotate stock and follow local regulations. Do not store near incompatible materials. Maintain good housekeeping.
    Shelf Life Shelf life is typically 12 months when stored unopened in original packaging, dry, cool, and away from direct sunlight.
    Application of TPC (Japan) HDPE KS178A

    On a 500 mm twin-station shuttle blow molder producing 25 L tight-head HDPE jerrycans, the TPC (Japan) HDPE KS178A melt is maintained at a head temperature of 205–215°C, with feed-zone setpoint 170°C and die bushing 190–200°C. Parison programming shifts the die gap from 1.8 mm at the neck to 4.3 mm across the lower sidewall to counteract a measured hang-time sag of 12–16 mm/s; pre-blow air is 0.08–0.12 MPa and main blow air is 0.7–0.9 MPa. Mold coolant enters at 10–14°C and the overall cycle time is 58–72 s for a 2.7 kg shot. Pinch-off flash is held below 0.6 mm by trimming tool depth to reduce granule size variability in closed-loop regrind.

    Formulation addition ratios are metered gravimetrically. The pellet is dry-blended with 2.0–3.0 wt% carbon black masterbatch, 0.05–0.15 wt% hindered phenolic antioxidant, 0.10–0.30 wt% antistatic concentrate for solvent packaging below 10-8 S/m surface conductivity, and 0.05–0.10 wt% calcium stearate as an acid scavenger. Regrind from tail flash and rejected containers is screened through 60/80/100 mesh and introduced at 15–30 wt%; the compound remains within the drop-tested melt strength band until regrind exceeds 40 wt%.

    Regulatory compliance for dangerous-goods packaging follows 49 CFR 178.509, ADR 6.1.5, and the IMDG Code 6.1; food-contact applications are evaluated under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011. Sidewall thickness is verified by ultrasonic gauge at four quadrants with a tolerance of ±0.3 mm on the sidewall and ±0.5 mm at the pinch-off. Terminal products include 20 L and 25 L UN 1H2 jerrycans, 30 L narrow-mouth agricultural adjuvant containers, and 5–10 L handled bottles for water-based latexes where the grade has been qualified against ASTM D1693 environmental stress-crack resistance.

    When coextrusion blow molding positions KS178A as the structural outer layer in agrochemical barrier packaging

    Six-extruder sequential coextrusion of 10 L multilayer jerrycans uses KS178A in the outer skin and in the regrind-containing carrier layers, with mass fractions of 12–18% outer HDPE, 35–50% regrind HDPE, 2–3% tie resin, 3–5% EVOH, 2–3% tie resin, and 15–20% inner HDPE. The outer layer is dry-blended with 2.0–4.0 wt% color masterbatch and 0.05–0.20 wt% antioxidant; the inner layer contains 1.5–2.5 wt% white masterbatch to provide visual contrast against the fill level. EVOH is pre-dried at 80°C for 4–6 h to a moisture content below 0.05 wt%, while KS178A requires hopper moisture below 0.05 wt% only when the ambient relative humidity exceeds 60%.

    The die head is profiled from 220°C at the outer HDPE layer to 205°C at the EVOH layer to control viscosity mismatch and prevent interfacial waviness near the pinch-off. Blow air is 0.8–1.2 MPa and mold water is 8–15°C; the 10 L container cycle is 75–95 s. Wall thickness is fixed at 1.2–1.6 mm in the sidewall and 2.2–2.8 mm at the handle pinch area, with the EVOH layer thinned by 30–50% at weld lines but maintained above 1.5% of total wall in the top-load-bearing sections.

    Dangerous-goods qualification for the multilayer container follows UN 3H2 design type testing under 49 CFR 178.509 and ADR 6.1.5; agrochemical compatibility is screened by comparing mass change and elongation loss under ASTM D543-21 after 30 days exposure at 40°C to xylene, cyclohexanone, and formulated emulsifiable concentrates. Food-contact status of the inner layer is assessed under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011. Terminal products include 5 L, 10 L, and 20 L multilayer jerrycans for solvent-based herbicides, emulsifiable concentrate pesticides, and adjuvants that require high oxygen barrier to prevent active ingredient oxidation.

    A grooved-feed single-screw extruder with 33:1 L/D and a 200 mm barrier screw feeds a corrugator producing 300 mm outside diameter double-wall drainage pipe under a 180–210°C barrel profile, 190–210°C die temperature, and 0.6–0.9 bar corrugator vacuum. KS178A is dry-blended with 2.0–3.0 wt% carbon black masterbatch to meet the carbon black dispersion and ultraviolet resistance clauses of AASHTO M294 and EN 13476-1; the compound is checked by ISO 18553 dispersion rating before startup. The pipe is sized in a corrugated mold-block system with 10–25°C block cooling, and the inner liner is extruded in the same pass with a die lip gap of 1.2–2.0 mm. Terminal products include 300 mm double-wall road culverts, agricultural drainage lines, and cable duct where compliance with ASTM F2306/F2306M is required.

    How Does Injection Blow Molding Translate Melt Elasticity into Wall-Thickness Uniformity in Medicinal Bottle Molding?

    The one-stage injection blow process raises KS178A melt in the injection barrel to 205–225°C, fills a preform cavity at 80–120 MPa injection pressure, and transfers the preform at 145–155°C to the blow station before blowing with 0.6–1.2 MPa air into a mold held at 8–12°C. Preform neck temperature is held 10–15°C below the sidewall to preserve thread dimensional stability; blow air is introduced through a 0.8 mm orifice tip to reduce jetting and asymmetric inflation.

    Formulation addition ratios for medicinal bottles are controlled by gravimetric dosing: 2.0–4.0 wt% white masterbatch with 60% TiO2, 0.05–0.15 wt% hindered phenolic antioxidant, and 0.05–0.15 wt% slip/antiblock concentrate. The target wall thickness is 0.4–0.9 mm for 30–100 mL bottles, with maximum deviation of ±0.10 mm in the seal area and ±0.15 mm in the sidewall measured by a vision wall-thickness gauge.

    Compliance for pharmaceutical use follows USP <661.1> and USP <661.2> extractables testing, Ph. Eur. 3.1.3, FDA 21 CFR 177.1520, and elemental impurity limits under ICH Q3D. Steam autoclaving above 121°C is not recommended for this HDPE grade; terminal products are therefore limited to 30 mL oral dosing bottles, 100 mL syrup bottles, and 10 mL ophthalmic dropper bottles that are sterilized by ethylene oxide or gamma irradiation at 25 kGy, where published data for this specific configuration is limited and requires lot-specific oxidative induction time testing.

    Geomembrane Sheet Extrusion: Carbon Black Dispersion, Roll Stack Friction, and Stress Crack Resistance

    A 120 mm single-screw extruder with L/D 30:1 and a barrier flight section feeds a 3.5 m flat sheet die for 1.5 mm smooth HDPE geomembrane. Barrel temperatures are set 195–220°C, die temperature 220–235°C, and the three-roll stack is held at 85–105°C to minimize residual stress; screen changer uses 40/60/80 mesh packs to remove gels. The KS178A pellet is dry-blended with 2.0–3.0 wt% carbon black masterbatch, 0.20–0.50 wt% antioxidant package, and 0.01–0.05 wt% fluoropolymer process aid. Carbon black dispersion is verified by ISO 18553 and by microtome inspection at 20× magnification before wound rolls are released.

    Compliance with landfill liner specifications follows GRI-GM13 for smooth 1.5 mm HDPE geomembrane: nominal density under ASTM D1505 is typically above 0.940 g/cm³, tensile break strength under ASTM D6693 is expected to exceed 27 kN/m, elongation at break exceeds 700%, and stress-crack resistance under ASTM D1693 Condition C is evaluated for ≥500 h in the sheet machine direction and transverse direction. Thickness tolerance is maintained at ±5% by a beta gauge feedback loop. Terminal products include 1.0–2.5 mm geomembrane rolls for landfill basal liners, mining heap leach pads, and pond liners where low-temperature flexibility at −20°C is qualified by ASTM D1790-based brittleness testing.

    For Coextruded Fuel Tanks Installed on Small Off-Road Engines, Low-Temperature Drop Impact Drives Mold Cooling Design

    Multi-layer coextrusion blow molding of 10 L fuel tanks places KS178A in the outer and inner HDPE layers with an EVOH barrier layer at 2–4% of total wall thickness and tie layers at 1.5–2.5%. The outer layer is dry-blended with 1.5–2.5 wt% carbon black masterbatch and 0.15–0.30 wt% UV stabilizer; the inner layer contains 0.05–0.15 wt% acid neutralizer to reduce fuel oxidation by-product attack. Melt temperature is 205–225°C, die head 220–230°C, mold coolant 6–10°C to increase cooling stress at pinch-off and improve low-temperature drop-impact resistance.

    Permeation compliance for small off-road engine fuel tanks is tested under EPA 40 CFR Part 1054 or CARB EVAP using fuel C at 28°C and 40°C; the EVOH layer must remain continuous at corners and pinch-off, with minimum wall in EVOH of 0.5% of total wall thickness. Drop-impact qualification is performed on filled 10 L tanks at −40°C from 1.2 m onto a concrete impact surface; failure at the sidewall-thread interface occurs when local wall thickness falls below 1.5 mm. Terminal products include 5–20 L fuel tanks for lawnmowers, generator sets, outboard engines, and compact construction equipment.

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