E Polymers Eflex Hdpe M300

E-Polymers EFLEX HDPE M300

    • Product Name: E-Polymers EFLEX HDPE M300
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 924786
    Density 0.958 g/cm3
    Melt Flow Rate 0.30 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 28 MPa
    Elongation At Break 600%
    Flexural Modulus 1200 MPa
    Vicat Softening Temperature 125 °C
    Heat Deflection Temperature 70 °C at 0.46 MPa
    Environmental Stress Crack Resistance >1000 h
    Hardness 65 Shore D
    Melting Point 130 °C
    Water Absorption <0.01%
    Thermal Conductivity 0.45 W/m·K
    Coefficient Of Linear Thermal Expansion 1.2E-4 /°C
    Volume Resistivity >1E16 Ω·cm
    Dielectric Constant 2.3

    As an accredited E-Polymers EFLEX HDPE M300 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing E-Polymers EFLEX HDPE M300 is supplied in 25 kg polyethylene-lined woven bags, palletized and stretch-wrapped for industrial storage.
    Container Loading (20′ FCL) 20′ FCL container loaded with E-Polymers EFLEX HDPE M300 in 25 kg bags, palletized, shrink-wrapped, and securely stowed for export.
    Shipping E-Polymers EFLEX HDPE M300 is a non-hazardous high-density polyethylene resin. Ship in original sealed bags, octabins, or bulk containers, protected from moisture, UV, and contamination. No special transport classification required; follow standard dry-cargo handling and local regulations. Keep away from ignition sources and store in cool, dry, ventilated areas during transit.
    Storage Store E-Polymers EFLEX HDPE M300 in original, sealed packaging in a cool, dry, well-ventilated area. Protect from direct sunlight, heat, moisture, and ignition sources. Keep away from incompatible chemicals and oxidizers. Prevent dust accumulation and static discharge. Use first-in, first-out rotation, maintain clean handling equipment, and follow the manufacturer’s SDS and local regulations.
    Shelf Life Shelf life: about 24 months in original unopened packaging, stored cool, dry, ventilated, away from direct sunlight and moisture.
    Application of E-Polymers EFLEX HDPE M300

    In high-cavitation closure manufacturing, EFLEX HDPE M300 is processed in hot-runner injection molds where the dominant constraints are gate freeze-off, part ejection, and dimensional stability across a 0.55–1.10 mm sidewall. Melt plastication is carried out on reciprocating screw injection units with L/D ratios of 20:1 to 24:1 and compression ratios between 2.0:1 and 2.8:1. The melt temperature measured at the nozzle is controlled within 190–235°C, while the chilled water circuit maintains cavity steel at 10–25°C. Under these conditions the crystallization front propagates rapidly enough to permit demolding of closures in 4–10 s, but the process is vulnerable to cold-flow defects if the melt temperature falls below 190°C, particularly in multi-cavity runner systems with uneven shear heating. Application-critical tests for closures include strip torque per ASTM D3198, stress-cracking resistance per ASTM D1693, and overall migration per EU Regulation 10/2011 for food-contact use. In pharmaceutical closures, FDA 21 CFR 177.1520(c) establishes the olefin polymer compliance basis, while current good manufacturing practice under EU Regulation 2023/2006 applies to all food-contact plastic operations. For colored systems, addition of a PE-based white or tint masterbatch at 1.0–2.5 wt% is typical; nucleating agents are avoided in closure formulations because excessive nucleation in thin walls increases warpage and ovality. Published production data for this exact commercial grade in high-cavitation closure tooling remains limited, so the processing envelope should be verified by short-shot studies and mold-pressure transducers before commissioning.

    PropertyTest/StandardAcceptance frame
    Application torqueASTM D3198Closure-specific; tamper-evident band removal torque
    Stress crack resistanceASTM D1693No brittle failure within qualification window
    Overall migrationEU Regulation 10/2011<10 mg/dm²
    Olefin complianceFDA 21 CFR 177.1520(c)Conditions of use A–H per food type
    Melt flow rateISO 1133-1:2022Medium-flow injection envelope; virgin baseline

    How Does Differential Shrinkage Constrain Stackable Crate Tooling?

    Stackable crates and distribution trays are molded from EFLEX HDPE M300 in single- or dual-cavity tools with wall thicknesses between 2.5 mm and 4.5 mm and rib-to-wall ratios kept below 0.6:1 to avoid sink marks. Shrinkage measured per ISO 294-4 in the flow direction typically falls in the range 1.5–2.5%, while transverse shrinkage can be 0.2–0.6 percentage points higher; this differential produces corner lifting and bottom warpage when packing pressure is released too early. The corrective process sequence is therefore not uniform: gate freeze is delayed by holding pressure at 55–75% of peak injection pressure for 8–20 s, after which cooling time is extended to 25–45 s depending on nominal wall. Low-temperature abuse tests on crates are performed to ISO 179-1/1eA at –20°C, with failures commonly initiating at the junction between side wall and bottom grid rather than at the gate. Because regrind from runner systems and rejected crates is often recompounded at 20–30 wt%, the molding technician monitors melt flow index per ISO 1133-1:2022 at 190°C under 2.16 kg load; an upward drift in MFI above the virgin resin baseline indicates molecular weight reduction from repeated shear and thermal cycles. The processing boundary for EFLEX HDPE M300 is established by balancing the need for high injection speed to fill the rib structure against the risk of jetting and weld-line weakness at the central stacking lug. If the melt is injected through a single central gate into an unvented tool, air traps at the last-filled bosses produce burn marks and local oxidative degradation; peripheral gates or sequential valve-gate actuation are preferred for crates with stack-load specifications greater than 300 kg per crate. Stack-load resistance is evaluated per ASTM D642 or ISO 12048, with acceptance thresholds defined by the end user rather than the resin supplier.

    When UN-Certified Industrial Pails Are Molded with EFLEX HDPE M300 at High Regrind Loads

    Industrial pails and jerry cans molded from EFLEX HDPE M300 require compliance with UN packaging performance tests when they are intended for regulated liquid transport. In this application, the resin is processed at melt temperatures of 210–245°C and cavity pressures of 45–70 MPa, with clamp force per projected area generally in the range 3.0–4.5 kN/cm². The critical manufacturing conflict is not filling but environmental stress crack resistance: contact with surfactants, oils, or mildly aggressive aqueous solutions can convert a properly molded pail into a brittle failure if molecular orientation near the gate is excessive or if weld lines are produced by multiple hot nozzles. ESCR testing is therefore performed according to ASTM D1693 in 10% Igepal CO-630 at 50°C, although end users frequently demand notched constant tensile load testing per ASTM D5397 for more severe service. Drop and stack tests follow the UN Model Regulations or local competent authority procedures; a typical 20 L pail of HDPE is conditioned to –18°C and dropped from 1.2 m at the closure seam and bottom chime. Stack compression after 24 h to 7 d at 40°C is evaluated per ASTM D642, with deformation limits set by closure seal integrity rather than absolute stack load. Regrind use in industrial pails can reach 30–40 wt% if the regrind is free of contamination and processed with a cushion position controlled to ±1 mm; otherwise shot-to-shot weight variation produces thin sections at the handle boss. The resin should not be dried unless visible surface moisture is present, and if drying is performed, a desiccant hopper dryer set at 80°C for 2 h is sufficient; higher temperatures risk pellet agglomeration in the hopper. Where color is required, the concentrate is kept below 3 wt% because high loadings of carbon black or titanium dioxide reduce low-temperature impact and increase pressure drop through the non-return valve.

    FunctionStandard/RegulationTest/conditioning detail
    Drop impact at cold seamUN Model Regulations 6.1.5.3–18°C, 1.2 m drop on bottom chime and closure seam
    Stack compressionASTM D64240°C, 24 h–7 d, deformation limit tied to seal integrity
    Environmental stress crack resistanceASTM D169310% Igepal CO-630, 50°C, condition as specified
    Notched constant tensile loadASTM D5397Severe service; user-defined stress and bath concentration

    Thin-walled food storage containers, reusable lunch boxes, and kitchen drawer organizers represent a separate production regime in which wall sections as low as 1.0 mm are combined with thick snap-fit hinges and sealing lips. EFLEX HDPE M300 is processed on standard injection machines with melt temperatures of 200–230°C and cooling water at 12–28°C; cycle time is limited by the thick hinge section, which can remain soft beyond 12–18 s and cause distortion during ejection. For food-contact articles, the finished item is tested for overall migration under EU Regulation 10/2011 Annex III using food simulant D2 or E for fatty contact and simulant A for aqueous contact; total migration must not exceed 10 mg/dm². Under US law, the base resin is subject to FDA 21 CFR 177.1520, and the finished houseware must comply with the applicable food-type and condition-of-use limitations in that section. EFLEX HDPE M300 does not contain intentionally added bisphenol A or phthalate plasticizers; acceptable compliance is demonstrated through screening gas chromatography-mass spectrometry after solvent extraction under the user’s own quality system. The molding facility controls odor and organoleptic transfer by purging the barrel after color changes and by avoiding excessive melt residence times above 5 min at 230°C, since thermal oxidation of unstabilized HDPE generates low-molecular-weight carbonyl species that migrate into fatty simulants. Mold release in deep-draw containers is assisted by a PE-compatible external mold release or by texturing the cavity surface to a VDI 24–30 roughness; internal release agents are generally avoided because they modify surface tension and compromise ultrasonic welding of the base to the lid. Published data for this specific grade in organoleptic testing is limited; therefore sensory evaluation panels according to ISO 13302 are recommended for each new masterbatch combination.

    Automotive Battery Container Ribs and Cable Duct Inserts

    Injection-molded battery containers and cable protection ducts use EFLEX HDPE M300 where a combination of low-temperature bridging strength and resistance to dilute electrolyte is required. The material is molded into ribs, end plates, and snap-fit cable channels with wall thicknesses from 1.5 mm to 3.0 mm. For battery applications, the resin is assessed for notched impact per ISO 180/A at –30°C after conditioning for 48 h; failures at the injection point are traced to internal weld lines caused by high-speed fill through a single gate. To avoid such failures, two or more tunnel gates are employed and the injection velocity profile is staged: a slower first-stage fill of 30–50 mm/s followed by a faster second stage of 80–120 mm/s reduces jetting at the rib intersections. Flame-retardant packages are generally not applied to EFLEX HDPE M300 in automotive cable ducts because the base resin is rated HB per UL 94 at 1.5 mm; when enhanced flame resistance is required, the molder must confirm additive compatibility because brominated systems in HDPE can plate out on mold steel and cause vent blockage. Compliance under REACH Annex XVII and the RoHS Directive 2011/65/EU Annex II is verified by X-ray fluorescence screening for restricted metals and by targeted GC-MS for restricted phthalates. Dimensional stability after thermal cycling from –40°C to 85°C is tested in accordance with the end user’s component specification, with post-cycle warpage often required to be below 1.0 mm for parts with uniform wall stock; uneven rib spacing can raise this to more than 2.0 mm. The specific application temperature limit for continuous service in air is bounded by the oxidative induction time measured per ISO 11357-6; at 85°C, long-term stabilizer depletion becomes the controlling degradation mechanism rather than mechanical creep. Published production data for EFLEX HDPE M300 in automotive battery container service is limited, so component validation should include field aging under actual under-hood thermal load.

    Material Handling Bins and Totes Demand Regrind-Tolerant Rheology

    Large rectangular totes, distribution trays, and interlocking bins are molded from EFLEX HDPE M300 in tools with shot weights up to 2–5 kg and wall thicknesses from 3.0 mm to 6.0 mm. The injection machine barrel capacity should be sized so that the shot uses 40–70% of maximum capacity to limit residence time; if the shot size is too small relative to barrel volume, prolonged contact with the screw root at 220–240°C accelerates thermomechanical degradation. In these thick sections, cooling time dominates cycle economics and scales with the square of wall thickness; a shift from 3.0 mm to 5.0 mm nominal wall can increase cooling time from 20–30 s to 60–120 s, depending on mold temperature. Dimensional stability of interlocking features is evaluated on a coordinate measuring machine after 24 h conditioning at 23±2°C and 50±5% RH; acceptance limits are typically ±0.5 mm on overall length and ±0.2 mm on rib spacing. For industrial totes used in automated storage systems, flatness of the bottom panel is the key performance attribute; warpage arises from differential shrinkage between the thick corner posts and the thin side walls. Gate placement at the side wall rather than the bottom center reduces visible flow marks and lowers the incidence of bottom corner cracking during drop tests. The melt flow rate of virgin EFLEX HDPE M300 and the diluted regrind stream is monitored per ISO 1133-1:2022; a shift of more than 0.5 g/10 min from the virgin baseline generally indicates that the regrind fraction contains degraded material or contamination from another resin. These bins are often exposed to outdoor UV radiation during storage; ultraviolet stabilization of EFLEX HDPE M300 requires a compounded hindered amine light stabilizer and a UV absorber package, and the pigment must be selected for weatherability rather than simple aesthetics. Because published comparative weathering data for this exact grade is limited, accelerated QUV testing per ISO 4892-2 is recommended for each specific color and wall thickness.

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    Certification & Compliance
    More Introduction

    E-Polymers EFLEX HDPE M300 is a high-density polyethylene grade whose alphanumeric designation separates the EFLEX family identifier from the M300 melt-flow-class suffix. In HDPE nomenclature, the M300 suffix is conventionally read as a nominal 0.30 g/10 min melt mass-flow rate class; however, the lot-specific ISO 1133-1:2022 value should govern all molding and extrusion decisions. The resin is presented as a black-compounded, high-molecular-weight HDPE for pressure-rated pipe, geosynthetic liner, and large-profile extrusion applications. Published data for this specific configuration is limited; therefore, the sections that follow pair standard HDPE reference data with lot-certificate requirements rather than substituting generic datasheet values for the manufacturer’s analytical report.

    The specification block that should accompany EFLEX HDPE M300 includes melt mass-flow rate, density, carbon black content, carbon black dispersion, tensile yield stress, slow crack growth resistance, hydrostatic design basis, and MRS classification. Each field is governed by a separate test method; the most frequently misinterpreted field is melt flow rate because the selection of 5 kg or 21.6 kg nominal load changes the numerical result by an order of magnitude. For high-molecular-weight pipe grades, the 21.6 kg load is the more informative control because the 5 kg load may return values below the practical measurement window.

    A Bimodal Molecular Weight Distribution That Shifts the Failure-Time Curve

    The M300 designation, when interpreted within the EFLEX HDPE family, is associated with a bimodal molecular weight distribution. Low-molecular-weight chains contribute shear-thinning and melt flow, while high-molecular-weight chains provide slow crack growth resistance and long-term hydrostatic strength. The density range typical for HDPE pipe and sheet grades spans 0.945–0.965 g/cm³ under ISO 1183-1:2019; melt flow rate determined under ISO 1133-1:2022 at 190°C with the selected load differentiates extrusion grades from injection grades. Product-specific melt flow rate values should be taken from the lot certificate.

    The difference between E-Polymers EFLEX HDPE M300 and lower-molecular-weight HDPE grades is not merely viscosity; it appears in the slope of the slow crack growth curve under ISO 13479:2022 and in the hydrostatic design basis under ISO 9080:2022. For pressure pipe, a bimodal HDPE resin with a high-molecular-weight tail generally provides an extrapolated long-term hydrostatic strength that permits a 10 MPa design stress when certified as PE100. If the grade is certified to a lower MRS class, the design stress follows the relevant ISO 12162:2009 classification.

    Moisture exposure during silo storage or pneumatic conveying is a processing variable, not a cosmetic issue. For HDPE, moisture levels below 0.05 wt% do not require pre-drying; however, if ambient relative humidity exceeds 60% during storage of regrind-laden feedstock, surface condensation can produce surface defects in extruded sheet and pipe. The safe response is closed-loop hopper drying at 70–80°C for 2–3 h or use of a vented barrel. Low-level water contamination does not hydrolyze HDPE the way it damages polyesters, but it collapses melt homogeneity at the die lip.

    If Melt Temperature Exceeds 220°C in a 33:1 L/D Grooved-Barrel Extruder, Which Degradation Mechanisms Appear First?

    Extrusion of high-molecular-weight HDPE on single-screw extruders with 30:1 to 36:1 L/D ratios and grooved feed sections is limited by localized viscous dissipation at the screw tip and mandrel. A typical barrel temperature profile for a high-molecular-weight pipe grade starts at 180°C in the feed zone, rises to 200–210°C in the compression zone, and holds at 210–215°C at the metering zone and adapter. If the melt temperature exceeds 220°C, the rate of thermo-oxidative chain scission accelerates. The first observable indications are usually gel particles in the extrudate, followed by surface sharkskin and reduced hydrostatic burst pressure in finished pipe.

    Under ISO 11357-6:2018, oxidative induction time at 210°C in oxygen typically measures between 20 and 60 min for formulated HDPE pipe compounds, but residual OIT below 10 min is often associated with gel formation and dimensional instability. Melt temperature is therefore not a parameter to be increased casually to reduce viscosity. If head pressure rises above the extruder safety limit, the correct interventions are screw-speed adjustment, die-land modification, or regrind ratio reduction. Reclaimed HDPE of unknown stabilizer history should be limited to 10–15 wt% until verified by ISO 11357-6:2018 and ISO 18553 carbon black dispersion testing.

    In grooved-barrel machines, the high feed-zone pressure can generate nonuniform solids-bed breakdown when the screw is worn. Screw and barrel wear should be monitored against the original clearance; a diametral wear allowance exceeding 0.25 mm can reduce melt homogeneity without triggering obvious alarms. The use of a barrier screw with intensive mixing elements improves dispersion but also raises melt temperature by 5–10°C; therefore, a barrel profile 5°C below standard may be required when converting to a high-shear screw.

    Using Melt Strength and Die Swell to Distinguish Bimodal M300 from Unimodal PE80

    Unimodal PE80 grades exhibit lower die swell and lower melt strength than bimodal PE100 grades at comparable shear rates. The M300 grade, if it follows the EFLEX bimodal pattern, is expected to show shear thinning that permits stable extrusion of thick-wall pipe while retaining a high zero-shear viscosity. Capillary rheometry on a twin-bore apparatus under 190°C and 210°C across shear rates 10–1000 s⁻¹ is the appropriate comparative test; no single melt flow value captures the difference. Melt strength can be estimated from the exit pressure or from a lab-scale sag test using an extruded strand at 200°C.

    Compared to a unimodal HDPE extrusion grade of the same nominal melt flow rate, the bimodal M300 architecture shifts the viscosity curve upward at low shear and downward at high shear. This creates processing differences: lower motor load in high-shear extrusion, but higher head pressure at low throughput. The practical consequence is that a grooved-barrel extruder optimized for a unimodal PE80 may need a different screw profile when converting to M300. The difference also appears in parison sag during large-part blow molding; bimodal grades typically hold the parison longer, allowing heavier shot weights without excessive thinning.

    Pressure pipe manufactured from EFLEX HDPE M300 is designed around the ISO 12162:2009 material class rather than the raw tensile yield value. For PE100 class material, the minimum required strength at 20°C is 10 MPa; for PE80, it is 8 MPa. The grade should not be placed in continuous chlorinated water service without verifying that the stabilizer package and slow crack growth profile meet chlorine-specific requirements. Chemical resistance follows HDPE norms: the material is resistant to dilute aqueous acids, alkalis, and polar solvents at ambient temperature but is not recommended for strong oxidizers, aromatic hydrocarbons, or chlorinated hydrocarbons at elevated temperature due to swelling, permeation, and environmental stress cracking.

    When Chemical Contact Shifts from Drinking Water to Aggressive Hydrocarbons, the Design Margin Narrows

    Compliance for EFLEX HDPE M300 is application-specific and temperature-dependent. In drinking water and food-contact applications, the finished article must comply with FDA 21 CFR 177.1520 or the relevant national list for polyethylene olefin polymers. REACH and RoHS declarations apply to the compounded resin, but only the full formulation disclosure can establish whether the stabilizer and carbon black packages satisfy migration limits. The resin should not be combined with polyamide or EVOH barrier scrap without a dedicated tie-layer strategy; phase separation creates delamination in pipe walls. Blending with polypropylene at low melt temperature is also unfavorable because the two phases can reduce impact strength.

    The table below identifies the normative data fields that should appear on a lot acceptance document or certificate of analysis. Absence of any field is a supply-chain risk, not a routine variation.

    Data fieldNormative referenceTypical test conditionLot acceptance output
    Melt mass-flow rateISO 1133-1:2022190°C, 21.6 kg or 5 kg as specifiedLot-specific MFR
    DensityISO 1183-1:201923°CBase density
    Carbon black contentISO 6964Oxidative pyrolysis2.0–2.5 wt% for UV-stabilized pipe grade if applicable
    Carbon black dispersionISO 18553Microtome film scanMaximum particle size and undispersed agglomerate rating
    Tensile yield stressISO 527-2:2012 or ASTM D638-1450 mm/min, Type 1 or Type IVLot-specific value
    Slow crack growthISO 13479:202280°C, notch pipe testTime to failure
    Hydrostatic design basisISO 9080:202220°C, 60°C extrapolationLong-term hydrostatic strength
    MRS classificationISO 12162:2009Minimum required strengthPE80, PE100, or lot-specific

    In service, continuous exposure to strong oxidizers or to hydrocarbons with high permeation rates reduces the effective design stress. The published data for this specific configuration is limited; therefore, any substitution of EFLEX HDPE M300 into a corrosive chemical environment should be preceded by immersion testing under ISO 4433-1 or an equivalent end-user protocol. The operational boundary is not defined by the polymer’s short-term tensile strength but by the slow crack growth resistance retained after chemical uptake.

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