Chase Plastics Hdpe Pe 200 Hd8m

Chase Plastics HDPE PE-200-HD8M

    • Product Name: Chase Plastics HDPE PE-200-HD8M
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 681442
    Density 0.955 g/cm3
    Melt Flow Rate 8.0 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 26 MPa
    Tensile Strength At Break 22 MPa
    Elongation At Break 1000%
    Flexural Modulus 1.2 GPa
    Notched Izod Impact 80 J/m
    Shore D Hardness 65
    Vicat Softening Temperature 125°C
    Heat Deflection Temperature At 0 45 Mpa 75°C
    Thermal Expansion Coefficient 1.3E-4 cm/cm/°C
    Water Absorption 0.01%
    Thermal Conductivity 0.40 W/m·K
    Melting Point 130°C
    Ul 94 Flammability Rating HB

    As an accredited Chase Plastics HDPE PE-200-HD8M factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Chase Plastics HDPE PE-200-HD8M is packaged in 50 lb (22.7 kg) multiwall bags, palletized for convenient industrial handling.
    Container Loading (20′ FCL) Chase Plastics HDPE PE-200-HD8M: 20′ FCL holds 800 x 25 kg bags, 20 pallets, 20 MT net, shrink-wrapped and secured.
    Shipping Shipping description for Chase Plastics HDPE PE-200-HD8M: non-hazardous high-density polyethylene resin, not regulated as dangerous goods by DOT/IMDG/IATA. No UN number, hazard class, or packing group. Transport in sealed bags, boxes, or octabins; keep dry, clean, and away from excessive heat. Handle as industrial plastic pellets.
    Storage Store Chase Plastics HDPE PE-200-HD8M in a cool, dry, well-ventilated warehouse. Keep containers sealed, labeled, and palletized off the floor. Protect from moisture, dust, contamination, direct sunlight, extreme heat, and ignition sources. Keep away from strong oxidizers, acids, and bases. Ensure adequate ventilation during handling. Avoid static discharge. Use FIFO stock rotation, inspect containers regularly, and follow the SDS.
    Shelf Life Shelf life: typically indefinite if stored cool, dry, sealed, and away from heat, sunlight, moisture, and contamination in original packaging.
    Application of Chase Plastics HDPE PE-200-HD8M

    Application screening for Chase Plastics HDPE PE-200-HD8M is governed by lot certificate values for melt mass-flow rate, density, molecular weight distribution, and comonomer type. Each downstream scenario below identifies the process window, formulation ratio, regulatory clause, and terminal article only where the supplied lot meets the stated MFR and density bounds. Published data for this specific configuration is limited in some conversion sectors; qualification trials remain the acceptance authority when lot-level data diverges from the cited industrial range.

    Extrusion blow moulding of tight-head UN-rated containers places the highest environmental stress crack resistance demand on HDPE. When PE-200-HD8M is evaluated on a 60 mm 24:1 L/D grooved-barrel extruder with a barrier screw and a single-head blow pin, melt temperature is constrained between 190 °C and 215 °C to limit parison drawdown. A die gap of 1.8 mm to 2.5 mm and blow air pressure of 0.6 MPa to 0.9 MPa are used for 10–25 L containers; wall thickness distribution is verified by sectioning at the handle pinch-off and the bottom chime. Parison swell is measured by capillary rheometry under ISO 11443; a die swell ratio outside 1.5–2.2 indicates excessive shear history and requires screw or die land adjustment. The resin requires pre-drying only if storage RH exceeds 60 %, as surface moisture produces splay but does not hydrolytically degrade the polyolefin backbone. Regrind from flash and tail trim is incorporated at 15–20 wt% provided the regrind is free of barrier-layer contamination. Container compliance for dangerous goods is evaluated under UN 1H2/Y stack load, hydraulic pressure retention at 100 kPa for 30 min, and drop impact at −18 °C according to UN 6.1.5.3. Terminal articles include 20 L UN jerricans, agricultural chemical barrier bottles with a polyamide or fluorinated inner layer at 3–6 wt% of the total wall, and automotive auxiliary fluid reservoirs.

    Pressure Pipe Extrusion Demands a Narrow Carbon Black and Antioxidant Window

    In pressure pipe extrusion on a 75 mm 30:1 L/D grooved-feed single-screw extruder, melt temperature is held between 200 °C and 225 °C for PE-200-HD8M when the lot certificate reports an MFR of 0.2–0.7 g/10 min under ISO 1133-1:2022 condition T. Carbon black masterbatch is let down at 5.5–6.5 wt% to achieve a final carbon black content of 2.0–2.5 wt% per ISO 4427-2; carbon black dispersion is rated against ISO 18553, and any agglomerate above 0.5 mm requires screen pack replacement. Antioxidant retention is critical because stagnant flow at the spider legs can consume hindered phenolic stabilizer before hydrostatic testing. Extrusion rate on a 250 mm diameter SDR 21 pipe is controlled by cooling length rather than screw output; vacuum calibration at −0.03 MPa to −0.06 MPa and haul-off speed are balanced to maintain wall thickness at 10.0 ± 0.5 mm. A batch-to-batch MFR shift of 0.1 g/10 min typically requires a die temperature adjustment of 3–5 °C to prevent melt fracture at the inner lip. If the lot does not carry an MRS classification of PE100 or PE80, the pipe is limited to non-pressure drainage or ducting. North American potable water approvals are verified against NSF/ANSI/CAN 61. Terminal products include potable water distribution pipe certified to ISO 4427-2, irrigation mainlines, and low-pressure slurry transport lines.

    When Wedge Welding Geomembrane Seams, What Peel and Shear Values Govern Acceptance?

    Geomembrane liner extrusion uses a flat die with a 1.0–2.5 mm sheet thickness range and a chill-roll stack maintained at 70–90 °C. PE-200-HD8M intended for liners is dry-blended with 2–3 wt% carbon black masterbatch and a hindered phenolic/phosphite stabilizer package before feeding; the final sheet is checked for oxidative induction time at 200 °C by ASTM D3895-19, with values below 100 min considered unacceptable for exposed cover installations. Hot-wedge welding uses a wedge temperature of 400–430 °C, seam overlap 40–50 mm, and travel speed 1.2–2.0 m/min; the wedge is gapped to produce a squeeze-out bead of 1–2 mm width on both sides. Destructive seam testing at shift start requires shear failure in the parent sheet rather than in the seam plane and peel strength no lower than 80 % of parent sheet tensile tear strength under ASTM D6392-12. Trial wedge parameters must be re-established for each lot because antioxidant package changes shift the heat-affected zone. Terminal products include landfill basal liners, heap leach pad liners, and secondary containment basins. Published data for this specific configuration is limited; field welders typically correlate destruct parameters on a 1.5 mm trial sheet before production welding.

    PropertyTest methodIndustrial acceptance window
    Melt mass-flow rateISO 1133-1:20220.3–0.7 g/10 min at 190 °C/21.6 kg
    DensityISO 1183-1:20190.945–0.965 g/cm³
    Carbon black contentISO 69642.0–2.5 wt%
    Oxidative induction timeASTM D3895-19>100 min
    Stress crack resistance F50ASTM D1693-15b>1000 h in 100 % Igepal

    For thin-wall industrial pail production on a 300 t direct-clamp injection moulding machine with a 20:1 L/D general-purpose screw, PE-200-HD8M is processed only when the lot MFR is within the 6–9 g/10 min window under ASTM D1238-20 condition 190 °C/2.16 kg. Melt temperature is set at 210–240 °C, mold coolant at 10–25 °C, and injection velocity at 80–120 mm/s. Transfer pressure is held at 70–100 MPa with hold pressure at 60–80 % of transfer until gate freeze; this reduces post-mould shrinkage variation. Tooling allowances are set after measuring linear mould shrinkage under ASTM D955-08(2014), which for PE-200-HD8M typically falls between 1.2 % and 1.8 %. Regrind from cold runners and rejected pails is incorporated at 15–30 wt% only after melt filtration through a 60 mesh screen to remove degraded skins. Pigment loadings above 2.0 wt% should be pre-dispersed because organic pigments can nucleate non-uniform shrinkage and warpage. Stackable pail drop resistance is evaluated under ASTM D2463-15; tensile yield strength of die-cut plaques is checked to ASTM D638-14. Food-contact pails require resin compliance with 21 CFR 177.1520(c) and total nonvolatile extractives below the applicable simulant migration limit. Terminal products include 5 L, 10 L, and 20 L open-top pails, vented logistic crates, and container lids.

    Rotational Moulding Shot Weight and Cooling Rate Boundaries

    Rotational moulding of bulk storage tanks with PE-200-HD8M is viable only when the supplied particle size distribution passes 35 mesh to 90 % minimum and dry flow is measured by ASTM D1895-96. Oven temperature is set at 280–320 °C with peak internal air temperature of 190–210 °C; operation above this peak accelerates inner-surface oxidation and reduces low-temperature impact. A biaxial rotational speed ratio of 4:1 with minor-axis speed 6–8 rpm maintains wall thickness uniformity for a 10 mm nominal wall. Cooling rate is limited to 8–12 °C/min during the crystalline solidification interval because faster cooling promotes warpage at baffle bosses and threaded inserts. The mould release agent is applied at 0.5–1.0 g/m² of mould surface; excess release causes pinholes at the inner surface. For outdoor exposure, a UV stabilizer masterbatch is added at 0.3–0.5 wt%. Low-temperature impact is verified after conditioning at −40 °C according to ASTM D1998-21. Oxidation induction time is re-checked on pulverized powder because grinding consumes antioxidant at the particle surface. Terminal products include 500–5,000 L vertical storage tanks, spill pallets, and agricultural chemical induction tanks.

    In cellular corrugation lines for agricultural drainage, PE-200-HD8M is processed on a 65 mm 24:1 L/D extruder feeding a water-cooled mould-block corrugator at melt temperature 190–215 °C and vacuum level 0.06–0.08 MPa at the block faces. The corrugator speed and extruder output are balanced to hold a minimum inner wall thickness of 0.6 mm and outer wall thickness of 0.8 mm; wall thinning at the valley radius is controlled by maintaining a melt strength above 0.15 N in a Rheotens test. Carbon black masterbatch is added at 2.0–2.5 wt% final content for UV resistance. Regrind from start-up and punching perforations is used at 10–20 wt%, but only after moisture content is reduced below 0.05 wt% to prevent surface pits on the corrugated wall. Condensation in the corrugator vacuum lines must be drained to avoid water spotting on the pipe OD. Pipe stiffness is measured to ASTM D2412-21, and impact resistance is verified by falling tup at 0 °C per ASTM D2444-20. Where the duct is used in electrical installations, RoHS compliance requires lead below 0.1 wt%, cadmium below 0.01 wt%, and hexavalent chromium below 0.1 wt%. Terminal products include 100–200 mm agricultural drain tile, cable duct, and landfill gas collection perforated pipe.

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    Certification & Compliance
    More Introduction

    Chase Plastics HDPE PE-200-HD8M is distributed as a high-density polyethylene injection-moulding resin. The grade is supplied in pellet form for thin-wall containers, caps, closures, housewares, and industrial pails in which high melt flow reduces injection pressure demand and improves cavity filling in long-flow-length tooling. Nominal density is 0.956 g/cm³ when determined under ASTM D1505-18. Melt flow rate is 8.0 g/10 min at 190 °C/2.16 kg using ASTM D1238-20. Mould shrinkage is typically 1.8–2.2 % after 48 h at 23 °C under ASTM D955-21, with higher values measured perpendicular to flow in edge-gated parts. The melt-flow position separates this grade from fractional-melt and high-molecular-weight HDPE used in blow moulding, film, sheet, and pipe; the resin is not a pipe-grade material under ISO 4427 or ASTM D3350.

    On production-scale toggle-clamp injection machines of 100–250 t clamp force, barrel temperature profiles from 190 °C to 230 °C reduce screw recovery torque without inducing pronounced yellowing. A general-purpose polyolefin screw with L/D 20–24 and compression ratio 2.5–3.0 is adequate; excessively high compression can raise stock temperature and lower viscosity below the target for cushion control. Injection velocity should be adjusted to achieve a fill time of 0.5–1.5 s in thin-wall tools; slower fill produces weld-line weakness and flow marks, while very high velocity above 250 mm/s can generate jetting in unvented pin gates. Packing pressure is held between 60–80 % of injection pressure for 4–8 s depending on wall thickness; insufficient packing produces sink marks above ribs and bosses, while excessive packing increases gate stress and demoulding force.

    Material drying is not required when the resin has been stored in intact bags at ambient relative humidity below 60 %; above 60 % RH, surface moisture should be removed in a desiccant dryer at 70 °C for 2–3 h. Regrind ratios of 20–30 % are common in non-food industrial containers, but closure and food-contact applications require lot-specific migration testing. The resin should not be processed above 250 °C for extended residence times, because molecular weight reduction increases odour and reduces environmental stress crack resistance. Hot-runner systems with valve gates or full-open sprue gates are preferred over small pin gates.

    How Does High-Flow HDPE Affect ESCR and Warpage in Thin-Wall Packaging?

    High-flow HDPE achieves lower molecular weight than blow-moulding grades; the resulting lower chain entanglement density reduces environmental stress crack resistance compared with fractional-melt HDPE. ESCR should be specified according to ASTM D1693-15 Condition B or ASTM F2136 for closures. If the application involves detergents, oils, or flavour emulsions, closure-grade ESCR testing under ASTM D1693-15 may be more predictive than generic HDPE data. Published data for this specific distributor designation is limited, and grade-specific ESCR must be obtained from the supplier. In thick-to-thin transitions, non-uniform cooling creates residual stress; a mould temperature of 15–40 °C is typical for fast cycles, but higher core temperatures of 50–70 °C reduce warpage at the cost of longer cooling time. Differential shrinkage measured by ASTM D955-21 can be 0.3–0.5 % higher in the flow direction; gate location and cooling channel balance control flatness better than extended holding pressure.

    Thermal, Mechanical, and Environmental Stress-Cracking Benchmarks

    Typical property profile for high-flow HDPE injection-moulding class
    PropertyTest methodNominal valueUnit
    DensityASTM D1505-180.956g/cm³
    Melt flow rateASTM D1238-20 (190 °C/2.16 kg)8.0g/10 min
    Tensile yield strengthASTM D638-14 Type IV28MPa
    Tensile elongation at breakASTM D638-14 Type IV300%
    Flexural modulusASTM D790-171.25GPa
    Notched Izod impactASTM D256-234.0kJ/m²
    Vicat softening temperatureASTM D1525-17127°C
    Mould shrinkageASTM D955-211.8–2.2%

    The values in the table are not specification limits and should be confirmed against the distributor’s certificate of analysis. Grade-specific lot-to-lot variation can shift tensile yield by ±1.5 MPa and flexural modulus by ±0.08 GPa depending on additive loading and pellet conditioning.

    When High-Flow HDPE Replaces Fractional-Melt Blow-Moulding Resins in Cap and Closure Tooling

    Tooling designed for fractional-melt HDPE with melt flow rate 0.3–0.7 g/10 min may require lower injection pressure and shorter fill with PE-200-HD8M, but the high-flow grade may also exhibit higher linear mould shrinkage and lower melt strength. In closure tooling, the higher flow improves thread detail and reduces short shots, but the lower molecular weight reduces strip torque and environmental stress crack resistance when exposed to aggressive oils and detergents. Caps with side gaskets or tamper-evident bands should be tested for tensile impact and seal integrity under ASTM D638-14 and ASTM D2463-15 drop impact. The high-flow grade is normally used in multi-cavity tools of 16–96 cavities; filling imbalance across hot-runner drops is controlled by gate geometry rather than raising barrel temperature. A melt temperature of 210–230 °C at the nozzle is recommended for minimal odour and maximum ESCR retention.

    Compliance with food-contact regulations requires verification of the base resin and additive package under the intended conditions of use. High-flow HDPE may be formulated with additives that are not approved for all food types; the moulding facility must obtain a written compliance letter. Under US FDA 21 CFR 177.1520, olefin polymers may be used in contact with food if the density and maximum extractable fraction meet the specified limits. Under EU Regulation 10/2011, overall migration must not exceed ≤ 10 mg/dm² for plastic food-contact articles. REACH candidate list declarations according to EC 1907/2006 and RoHS heavy metal limits under Directive 2011/65/EU should be confirmed at lot level.

    Regulatory and compliance matrix for high-flow HDPE injection moulding
    FrameworkStandard or clauseRequired verification
    US food contactFDA 21 CFR 177.1520Supplier compliance letter, end-use condition
    EU food contactRegulation (EU) 10/2011Overall migration ≤ 10 mg/dm²
    REACHEC 1907/2006SVHC candidate list declaration
    RoHSDirective 2011/65/EUHeavy metal concentration limits

    Storage under 40 °C and 60 % RH is recommended; opened bags should be sealed when not in use. The resin is incompatible with amine-based additives and certain peroxide masterbatches if used in reactive extrusion; oxidative chain scission can occur if exposed to copper-based catalysts in warm process water. Ultraviolet exposure is not intended for outdoor service beyond 1–2 years unless a stabilizer masterbatch is added. The grade is not suitable for continuous pressure pipe applications requiring hydrostatic design basis under ISO 4427 or ASTM D3350 PE4710/PE100 classifications.

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