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Lotte Chemical Titan HDPE HI2000

    • Product Name: Lotte Chemical Titan HDPE HI2000
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 870937
    Density 0.956 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 20 g/10 min
    Tensile Strength At Yield 28 MPa
    Tensile Elongation At Break >1000%
    Flexural Modulus 1200 MPa
    Notched Izod Impact Strength 40 J/m
    Vicat Softening Temperature 125 °C
    Heat Deflection Temperature 0 45 Mpa 75 °C
    Shore D Hardness 65
    Melting Temperature 130 °C
    Mold Shrinkage 1.5-3.0%
    Environmental Stress Crack Resistance >1000 h

    As an accredited Lotte Chemical Titan HDPE HI2000 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Lotte Chemical Titan HDPE HI2000 comes in 25 kg polyethylene bags or 1,000 kg jumbo bags for bulk handling.
    Container Loading (20′ FCL) Lotte Chemical Titan HDPE HI2000 in 20′ FCL: 25 kg bags, loose-loaded, approximately 20–22 MT net, dry container, standard secure stowage.
    Shipping Lotte Chemical Titan HDPE HI2000 is shipped as non-hazardous polyethylene pellets in 25 kg bags, jumbo bags, or bulk trucks/containers. Keep packaging dry, sealed, and protected from heat, sunlight, and moisture. Standard freight; no special hazardous-materials handling required. Store in cool, ventilated areas.
    Storage Store Lotte Chemical Titan HDPE HI2000 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and oxidizing agents. Keep original packaging sealed to prevent moisture, dust, and contamination. Use pallets, avoid excessive stacking, and maintain stable temperature. Protect from prolonged UV exposure. Keep away from incompatible materials. Follow local regulations and the manufacturer’s safety data sheet.
    Shelf Life Typically indefinite when stored in original unopened packaging, dry, away from direct sunlight, heat, and moisture, below 50°C.
    Application of Lotte Chemical Titan HDPE HI2000

    Dairy spread portion packs, frozen dessert tubs, and microwave-safe side-dish containers are injection-moulded in thin-wall tooling with nominal wall stocks between 0.45 mm and 0.70 mm. Direct food-contact grades must comply with FDA 21 CFR 177.1520(c) olefin polymer specifications and Commission Regulation (EU) No 10/2011 with overall migration below 10 mg/dm² under aqueous, acidic, and fatty simulats. Lotte Chemical Titan HDPE HI2000 enters this segment as a high-flow injection-moulding HDPE with a certified melt-flow rate of 20 g/10 min at 190 °C/2.16 kg tested to ISO 1133-1:2022, which allows filling of multi-cavity hot-runner tools at lower hydraulic pressure than conventional 8 g/10 min HDPE. On a 1600 kN hydraulic toggle machine with a 20:1 L/D general-purpose screw and a two-drop valve-gate hot-runner manifold, the melt profile is set at 195/205/215/220 °C from feed throat to nozzle, with the nozzle held at 225 °C to prevent gate freeze during valve sequencing. Injection speed is maintained at 120–160 mm/s, on-cavity hold pressure at 45–60 MPa for a hold time of 0.5–0.9 s, and mould coolant temperature at 15–25 °C. White masterbatch based on titanium dioxide in an LLDPE carrier is metered at 1.5–3.0 wt%; loadings above 3.0 wt% reduce weld-line tensile strength in the sidewall-to-base junction, as measured by ISO 527-2/1B. The main processing conflict is the narrow temperature window between complete cavity packing and oxidative gel formation: residence times above 20 min at melt temperatures above 235 °C increase visible black speck formation in translucent white tubs, while melt temperatures below 190 °C produce short shots in the 0.45 mm shoulder section on the same tool. For food-contact approval, the converter is responsible for verifying the final article under EU 10/2011 Annex IV migration testing with fatty simulants, not merely relying on resin certification.

    Compliance matrix for HI2000 downstream applications
    ApplicationRegulatory standard or test methodNumerical requirementBoundary condition
    Thin-wall dairy tubsFDA 21 CFR 177.1520(c) 3.2a; EU 10/2011OM 10 mg/dm²Final article migration testing required
    Still-beverage and dairy closuresFDA 21 CFR 177.1520(c) 3.2a; EN 1622:2006Organoleptic change threshold per EN 1622:2006Slip additive migration must be verified
    UN open-head pailsUN 1H2; ASTM D5276; ASTM D4577Drop 1.2 m at -18 °C; stack 24 h at 40 °CCarbon black maximum 2.5 wt%
    Ventilated cratesASTM D642; ISO 6603-2Top-load to ASTM D642 scheduleUV-stabilizer 2.0–3.5 wt% for outdoor service
    HousewaresEU 10/2011 if reusable kitchenwareOM 10 mg/dm²Not food-contact if non-kitchen article
    Aerosol overcapsFDA 21 CFR 177.1520(c) if food-contact closureNo single numerical value for non-foodDraft angle increase to 2–3° required

    What Limits High-Cavitation Closure Moulding with 20 g/10 min HDPE?

    Beverage closures with 30/25 mm neck finishes and tamper-evident bands are moulded in high-cavitation tools ranging from 64 to 144 cavities, using valve-gate hot runners and stack moulds. The processing target is not merely cavity filling; it includes gate freeze-off after packing, band stretching during ejection, and removal torque consistency on the finished closure. HI2000 is used at 100% resin for short-shelf-life still-water and dairy closures; for aggressive environments or higher ESCR, converters let down 5–15 wt% of a fractional-melt HDPE or a 1-butene copolymer with a density of 0.952–0.955 g/cm³ to raise environmental stress crack resistance. Slip masterbatch containing erucamide at 1.0–2.0 wt% is dosed separately to reduce cap-on-bottle torque; higher slip levels can migrate to the top sealing surface and cause seal leakage. Barrel profiles on a 2000 kN hybrid machine are set at 210/220/225/230 °C, hot runner at 230 °C, and mould chiller at 8–12 °C to freeze gates within 1.5–2.5 s. Injection velocity is set at 180–250 mm/s, with hold pressure limited to 35–50 MPa because higher hold pressures pack the tamper-evident band and increase ejection pin penetration. Cycle time is 6–9 s for 1.8–2.2 g shot weights. The gate quality is tested by dropping closures from 1.5 m onto concrete; brittle gate fracture indicates insufficient hold or excessive melt temperature. For child-resistant closures, final assembly is tested to ISO 8317:2015. Food-contact status is governed by FDA 21 CFR 177.1520(c) 3.2a and EU 10/2011; any organoleptic change in bottled water is evaluated under EN 1622:2006.

    UN 1H2 open-head pails, stacking load, and drop-test compliance

    In open-head pail production, the 20–25 L injection-moulded body is specified when dimensional stackability and closure integrity are required. HI2000 is formulated with 1.5–2.5 wt% carbon black masterbatch and 0.1–0.3 wt% of a primary/secondary antioxidant package; the high-flow base resin permits filling of the rim and bail-ear sections at 1.2–1.8 kg shot weights without excessive shear heating. Moulding is performed on an accumulator-assisted injection machine with a 2000–4000 kN clamp, a 120–150 mm screw, and a cold sprue bush feeding a ring gate near the pail rim. Barrel zone settings are 200/215/225/230 °C, melt cushion is kept below 5 mm, and mould temperature is controlled at 10–20 °C through turbulent-flow water channels. Injection pressure normally peaks at 90–120 MPa, with hold phase 50–70 MPa for 12–20 s; gate seal must be confirmed by weight stability across 10 consecutive shots. The UN 1H2 removable-head packaging designation requires conditioning and drop testing under ASTM D5276; the commonly cited test point for Packaging Group II solid materials is a 1.2 m free-fall onto a rigid steel plate after conditioning at -18 °C. Stacking performance is evaluated under ASTM D4577 at 40 °C for 24 h; pails made with HI2000 are typically filled to 75% of the maximum gross mass and stacked to 1.5 m height. Excessive carbon black above 2.5 wt% reduces low-temperature impact and creates visible weld lines at the bail-ear junctions.

    When HI2000 replaces 3–5 g/10 min HDPE in ventilated agricultural crates

    Bakery trays, mushroom crates, and beverage crates are injection-moulded as single-shot items with perforated sidewalls and integrated stacking lugs. The replacement of a 3–5 g/10 min HDPE with HI2000 allows the nominal wall thickness to be reduced from 2.5 mm to 2.2 mm, provided that top-load requirements are re-certified to ASTM D642. A typical ventilated mushroom crate with a 3.5 kg shot weight is processed on a 6500 kN machine at a melt temperature of 200–220 °C; the mould is cooled with water at 20–35 °C, and cycle time falls between 20 s and 30 s. For outdoor service, a UV-stabilizer masterbatch containing a hindered amine light stabilizer is dosed at 2.0–3.5 wt%, and carbon black is added at 2.0 wt% in parallel for black crates; the two masterbatches are metered separately to avoid pellet mixing errors. The principal processing limitation is warpage of the bottom deck: with the high-flow resin, the hold pressure should be reduced to 30–45 MPa and the mould temperature kept below 35 °C, otherwise post-ejection corner lifting exceeds 3 mm on a 600 mm long crate and is visible on flat-table inspection. Impact performance is checked with ISO 6603-2 puncture tests on the sidewall rib junctions; published data for this specific grade in ventilated crate geometry is limited, so the test report for the final moulded crate carries the compliance burden.

    Storage boxes with latch hinges, drawer organizers, and clothes hangers use HI2000 without filler or with 1.0–2.0 wt% colour masterbatch. The high melt-flow index permits filling of long draw cores for hanger hooks and latch undercuts at melt temperatures of 190–210 °C. Mould surface texture is the dominant variable controlling sink mark visibility; on polished cavities, gate blush appears at injection speeds above 150 mm/s, so speeds are limited to 80–120 mm/s. No food-contact testing is required in this segment unless the article is marketed as reusable kitchenware, in which case the final article is subject to EU 10/2011 and FDA 21 CFR 177.1520(c). Warpage of long flat lids is controlled by maintaining uniform cavity wall temperature within ±5 °C and by avoiding hold pressures above 40 MPa.

    Talc-filled overcap formulations and gloss-level control on textured cavity surfaces

    For aerosol overcaps, deodorant cap assemblies, and cosmetic jar closures, talc-filled HDPE compounds are used to increase modulus and reduce cycle time. HI2000 is let down with 10–20 wt% talc masterbatch and 0.5–1.0 wt% pigment masterbatch; talc additions above 20 wt% cause excessive gate wear and reduce weld-line elongation. The injection moulding machine is a 1000 kN hydraulic unit with a 20:1 L/D screw, running a melt temperature of 200–210 °C and a mould temperature of 15–25 °C. Textured cavity surfaces are vapour-honed or acid-etched; the high-flow base resin fills the texture at lower pressure than 8 g/10 min HDPE, but mould release becomes more difficult because the low-viscosity melt penetrates deeper into texture peaks. A mould-release agent is not used in food-contact overcaps; instead, draft angles are increased to 2–3° on sidewalls and the ejection speed is limited to 30–50 mm/s. The final article is tested for cap-on-bottle insertion force with a force gauge calibrated to 0.1 N.

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    Certification & Compliance
    More Introduction

    Lotte Chemical Titan HDPE HI2000 is a high-density polyethylene injection-molding grade supplied in pellet form. The material is defined by a nominal melt flow rate of 20 g/10 min at 190°C under 2.16 kg load in accordance with ASTM D1238, and a nominal density of 0.956 g/cm³ by ASTM D1505. These primary specifications place HI2000 in the high-flow segment of HDPE, where reduced melt viscosity permits short fill times and thin wall sections in discontinuous injection molding. The grade is not intended for blown film, sheet thermoforming, pipe extrusion, or blow molding processes that require high melt strength; its molecular architecture favors fast solidification and dimensional stability after ejection. The product is used principally in thin-wall containers, housewares, closures, toys, and caps where the combination of stiffness, flow length, and cycle time control is critical.

    What Rheological Parameters Differentiate HI2000 from General-Purpose Injection HDPE?

    The 20 g/10 min melt flow rate of HI2000 is substantially higher than the 6–12 g/10 min range common in general-purpose HDPE injection grades. The melt flow rate is measured on a dead-weight extrusion plastometer using a die diameter of 2.095 mm and die length of 8.000 mm under 2.16 kg load at 190°C, with equivalent determination possible by ISO 1133-1:2022. The elevated melt flow rate corresponds to lower average molecular weight and reduced chain entanglement density. In cavity filling, this produces lower injection pressure, faster flow-front advancement, and improved filling of wall sections that would freeze prematurely with lower-flow resins. However, the same molecular characteristics reduce melt strength and environmental stress-cracking resistance relative to high-molecular-weight HDPE grades. Because HDPE melt viscosity is non-Newtonian, the single-point melt flow rate does not fully describe viscosity at injection shear rates; capillary rheometry at shear rates above 1,000 s⁻¹ is required for mold-filling simulation. Published data for this specific grade at high shear rates is limited, but the general behavior of high-flow HDPE follows a pronounced shear-thinning profile.

    When HI2000 Is Melt-Prepared on Reciprocating-Screw Injection Molding Lines

    Processing of HI2000 follows the thermal and mechanical requirements of high-density polyethylene on reciprocating-screw injection machines. Typical melt-temperature settings for HDPE injection grades range from 180°C to 260°C, with rear zones near 180–200°C, center zones near 210–230°C, and nozzle zones near 220–240°C. Mold-surface temperatures between 10°C and 40°C are used to control shrinkage and ejection. Back pressure in the range of 0.5–1.5 MPa is generally sufficient to maintain a stable melt cushion without excessive shear heating. Screw geometries with compression ratios of 2.5:1–3:1 and L/D ratios of 18:1–22:1 are standard for HDPE injection. Pre-drying is not normally required when packaging is intact; if surface moisture or condensation is present, HDPE of this type can be dried for 2 h at 80°C. However, published data for this specific configuration is limited, and start-up trials should verify actual melt-temperature uniformity and cushion stability. On thin-wall tools with wall sections below 0.8 mm, a gate diameter below 0.8 mm may cause premature gate freeze before packing is completed. Production-scale molding experience with high-flow HDPE indicates that high injection velocity and short hold-time profiles are preferred to avoid flow hesitation at weld lines.

    Thin-wall containers and housewares molded from HI2000 often use wall thickness between 0.5 mm and 1.5 mm. The elevated melt flow rate allows longer flow paths at lower cavity pressure than general-purpose HDPE grades, but tooling must provide sufficient venting at flow-front meeting points. In closures and caps, the material is evaluated for hinge flexural life and torque retention; these properties depend on notched impact resistance and stiffness measured by ASTM D256 and ASTM D790. For food-storage containers, warpage control is influenced by cooling uniformity and mold temperature, with typical mold-side water temperature held at 20–30°C to balance cycle time against dimensional stability. A flow-length-to-wall-thickness ratio above 150:1 may require multiple gates or sequential valve-gate control to prevent short shots and excessive orientation. The resin is also used in toys and small appliance housings where ESCR testing under ASTM D1693 or ISO 22088-1 should be performed for formulations exposed to oils or surfactants.

    Mechanical Property Envelope at Yield and Impact Thresholds

    Representative manufacturer-published values for HI2000 are tabulated below. Production lots vary, and specification compliance should be verified against the current lot certificate. The mechanical property envelope reflects the expected balance of stiffness and impact resistance for a high-flow HDPE injection grade.

    Representative physical and mechanical properties of Lotte Chemical Titan HDPE HI2000
    PropertyTest methodValue
    Melt flow rateASTM D123820 g/10 min
    DensityASTM D15050.956 g/cm³
    Tensile stress at yieldASTM D63828 MPa
    Elongation at breakASTM D638>200%
    Flexural modulusASTM D7901,250 MPa
    Notched Izod impact, 23°CASTM D25640 J/m
    Vicat softening temperatureASTM D1525123°C
    Hardness Shore DASTM D224064

    The flexural modulus of 1,250 MPa provides stiffness in thin-wall parts without excessive brittleness, while the notched Izod impact value of 40 J/m at 23°C is adequate for non-safety-critical consumer articles. The elongation at break above 200% indicates ductile failure under tensile loading when the material is tested under standard specimen conditions. These values are not transferable to parts with sharp internal radii, weld lines, or high residual orientation; local stress concentrations can reduce practical impact performance below the notched-Izod result.

    Bimodal Pipe Resins and Blow Molding Grades Occupy a Different Molecular Architecture

    The molecular design of HI2000 differs from bimodal pipe resins and broad-molecular-weight-distribution blow molding grades. Bimodal HDPE pipe grades are compounded for PE100 pressure performance and exhibit melt flow rates below 0.5 g/10 min, higher environmental stress-cracking resistance, and broad to bimodal molecular weight distribution. Extrusion blow molding grades typically show melt flow rates from 0.25 g/10 min to 0.8 g/10 min to maintain parison melt strength and die swell. HI2000, at 20 g/10 min, has insufficient melt strength for continuous blow molding or pipe extrusion and should not be substituted into those processes without redesigned tooling and process settings. The table below summarizes qualitative differentiation across HDPE families.

    Differentiation between HI2000 and other HDPE product families
    ParameterHI2000 injection gradeExtrusion blow molding gradePressure pipe PE100 grade
    MFR 190°C/2.16 kg20 g/10 min0.25–0.8 g/10 min<0.5 g/10 min
    Density0.956 g/cm³0.953–0.960 g/cm³0.945–0.955 g/cm³
    Molecular weight distributionNarrowBroadBimodal
    Primary conversion processInjection moldingExtrusion blow moldingPipe extrusion
    Environmental stress-cracking resistanceLowerHighVery high

    Compliance under FDA 21 CFR 177.1520 and EU Regulation 10/2011 may apply to food-contact uses, but lot-specific certification and migration testing must be confirmed with the supplier for the intended food-simulant and temperature use. The resin should not be processed above 280°C, and prolonged residence time above 240°C may generate oxidative degradation products. The material is not recommended for sustained hydrostatic pressure applications, aggressive environmental stress-cracking environments, or continuous blow molding without specific validation. Substitution into pipe or blow molding equipment requires a different molecular architecture, higher melt strength, and stricter long-term hydrostatic qualification.

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