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Bayport Polymers (Baystar) HDPE 2287

    • Product Name: Bayport Polymers (Baystar) HDPE 2287
    • 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 459833
    Productname Bayport Polymers (Baystar) HDPE 2287
    Manufacturer Bayport Polymers (Baystar)
    Grade HDPE 2287
    Polymertype High Density Polyethylene (HDPE)
    Comonomer Hexene-1
    Density 0.954 g/cm3
    Meltindex 0.35 g/10 min (190°C/2.16 kg)
    Tensilestrengthatyield 25.5 MPa
    Tensilestrengthatbreak 30.0 MPa
    Elongationatbreak 600%
    Flexuralmodulus 1100 MPa
    Escr >1000 h (10% Igepal, F50)
    Hardnessshored 65
    Vicatsofteningpoint 126°C
    Brittlenesstemperature < -70°C
    Meltingpoint 130°C
    Processingmethod Blow Molding

    As an accredited Bayport Polymers (Baystar) HDPE 2287 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Typically supplied in 25 kg polyethylene bags or 1,000 kg bulk bags, with bulk truck shipment available.
    Container Loading (20′ FCL) 20′ FCL loaded with 25 kg bags of Bayport Polymers (Baystar) HDPE 2287 high-density polyethylene resin on pallets, securely lashed.
    Shipping Shipping description: Bayport Polymers (Baystar) HDPE 2287 is a non-hazardous high-density polyethylene resin. It is not regulated as dangerous goods under DOT, IMDG, IATA, or ADR. Transport in clean, dry, sealed bags, bulk bags, or bulk trucks/railcars. Keep containers closed; protect from moisture, contamination, and direct sunlight.
    Storage Bayport Polymers (Baystar) HDPE 2287 should be stored in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers/packages closed, clean, and palletized off the floor. Avoid moisture, contamination, and strong oxidizers. Maintain FIFO stock rotation. Protect from physical damage. Do not smoke. Use appropriate PPE when handling. Follow manufacturer SDS and local regulations.
    Shelf Life Shelf life: 24 months when stored in original unopened packaging under cool, dry, well-ventilated conditions, away from direct sunlight and heat.
    Application of Bayport Polymers (Baystar) HDPE 2287

    Thin-Wall Dairy Container Moulding Without Post-Consumer Recycle Loss of Injection Speed

    Bayport Polymers (Baystar) HDPE 2287 is specified where stackable single-serve dairy cups require wall sections between 0.6 mm and 0.9 mm without excessive injection pressure. The melt mass-flow rate used for lot release is 28 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg, and typical density under ISO 1183-1:2019 falls within 0.952 g/cm³ to 0.958 g/cm³. On production lines using accumulator-assisted hydraulic injection moulding machines with screw L/D ratios of 20:1 to 25:1, the melt temperature is held between 210 °C and 230 °C; mould temperature is kept between 8 °C and 18 °C to reduce cycle time and limit the sidewall crystallinity gradient. Injection velocity is set from 200 mm/s to 350 mm/s, hold pressure from 35 MPa to 55 MPa, and total cycle time from 4.5 s to 7.0 s for a 150 ml cup in a 32-cavity hot-runner tool. When the tool contains 32 or more cavities, passive runner balancing alone is insufficient; fill imbalance above 8% between first-filled and last-filled impressions can produce short shots and part weight variation beyond 0.15 g per impression. Valve-gate sequencing and artificial melt flippers are used to hold imbalance below 3%, which is the practical threshold for stable in-line rim leak testing. The formulation is normally neat HDPE 2287 with a food-contact white masterbatch at 2 wt% to 3 wt%, in which the titanium dioxide loading in the concentrate is 60% by weight on an LLDPE carrier; concentrate addition above 5 wt% is not recommended because melt-flow disturbances in the hot-runner manifold produce sidewall flow marks and inconsistent lid snap diameters. Regulatory conformity for direct food contact rests on FDA 21 CFR 177.1520(c), Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm², and GB 9685-2016 where colour concentrates are used. The terminal articles are single-serve yoghurt cups from 100 ml to 250 ml with snap-on lids; hot-fill above 85 °C is outside the recommended service envelope because stackability loss from sidewall creep exceeds 0.5 mm on a 150 ml cup. Post-consumer recycle let-down above 20 wt% requires a pre-production shear-sensitivity trial because melt pressure instability can exceed 1.2 MPa on a reciprocating screw if back pressure is not reduced.

    Because carbonated soft drink closures transfer melt across long hot-runner manifolds and gate into thin tamper-evident band sections, Baystar HDPE 2287 is processed at the upper end of its shear-rate range. Closure moulds typically run 48 to 96 cavities with valve-gate sequencing, melt temperature 220 °C to 240 °C, mould temperature 8 °C to 15 °C, and injection velocity 250 mm/s to 400 mm/s. Hold pressure on a 28 mm PCO 1881 neck closure is maintained at 40 MPa to 60 MPa for 0.8 s to 1.5 s, followed by cooling 3 s to 5 s; total cycle is 4.5 s to 7.5 s. The closure-side formulation uses 1.0 wt% to 2.0 wt% of a slip/anti-block masterbatch based on erucamide and silica, plus 2 wt% to 3 wt% of a colour concentrate; silicone oil levels above 0.2 wt% are controlled because cold-slip migration onto the scoring line can reduce tamper-evident bridge break consistency. Stress-crack resistance after carbonation at 3 bar to 4 bar CO₂ pressure is evaluated by brand owners using ASTM D1693-15, condition B, in 10% Igepal CO-630 at 50 °C; published comparative data for this specific grade are limited, so closure qualification is lot-specific and includes burst testing to 1.0 MPa minimum on filled bottles. Compliance covers FDA 21 CFR 177.1520(c), Regulation (EU) No 10/2011, EC 1935/2004 with organoleptic pass/fail under EN 1622 for water, and EU 2023/2006 good manufacturing practice for food-contact articles. The operational boundary is the tamper-evident band: when ambient warehouse temperature exceeds 40 °C, stored closures can relax bridge geometry and shift application torque outside 1.8 N·m to 2.5 N·m; inventory should be used first-expired first-out and not cooled below 5 °C immediately before capping because condensation on the linerless bore can generate cap-on-bottle application faults.

    What Limits the Maximum Stack Height for Injection-Moulded Crates Under Cold Chain Storage?

    Cold-chain crate failure is rarely a tensile yield event; it is a crack propagation problem initiated at gate or ejector locations after repeated stacking at -20 °C. Baystar HDPE 2287 is selected for dairy and bakery crates when wall thickness is 2.5 mm to 5.0 mm and the moulded part requires fast filling at moderate clamp force. On injection presses from 6,000 kN to 12,000 kN clamp force with shot capacities of 2 kg to 5 kg, the melt temperature is set between 210 °C and 240 °C; mould temperature from 15 °C to 25 °C is preferred for surface gloss and dimensional reproducibility. Injection velocity is deliberately reduced to 90 mm/s to 150 mm/s to prevent jetting in thick sections; hold pressure is 50 MPa to 70 MPa, hold time 8 s to 15 s, and total cycle 20 s to 35 s depending on rib density. Where cold-chain impact at -20 °C is specified under ISO 179-1:2010 Charpy notched conditions, an addition of 4 wt% to 6 wt% metallocene plastomer raises sub-zero impact energy but depresses hot stack performance at 40 °C; the resulting creep modulus loss can reduce permissible static stack height by 15% to 20% compared with the unmodified grade. UV-stabilized formulations for outdoor dairy crates use a hindered amine light stabilizer masterbatch at 1.5 wt% to 3.0 wt% and a carbon black masterbatch at 1.5 wt% to 2.5 wt% for black parts. Food-contact crate production follows FDA 21 CFR 177.1520(c) and Regulation (EU) No 10/2011; industrial crate production follows REACH Annex XVII and EU 2011/65/EU RoHS where electronic traceability tags are inserted. Gate design is the critical process boundary: edge-gate land length should not exceed 1.0 mm, and gate thickness below 2.0 mm creates high shear heating that generates splay marks and reduces weld-line strength at the base corners. The terminal articles are returnable bottle crates, bread trays, and dairy cases with service lives from 3 years to 8 years in closed-loop distribution.

    Open-head pail production on a 6,000-kN machine with a two-cavity tool running Baystar HDPE 2287 typically uses a melt temperature of 220 °C to 250 °C, mould temperature 12 °C to 20 °C, injection velocity 120 mm/s to 180 mm/s, and hold pressure 45 MPa to 60 MPa. For a 20-litre pail with a wall thickness of 1.8 mm to 2.5 mm, hold time is 6 s to 12 s and total cycle is 15 s to 25 s when the tool is cooled with turbulent-flow water lines at 10 °C to 15 °C and a Reynolds number above 4,000. The formulation is neat 2287 plus 2 wt% to 3 wt% colour concentrate; for agricultural or outdoor service, 1.5 wt% to 2.5 wt% UV masterbatch is added. The primary process defect is handle insert sink: a 3.0 mm steel wire insert in a 2.0 mm pail wall extends cooling time by 4 s to 6 s; if the machine is advanced early, tear-drop sink marks deeper than 0.05 mm form on the flat sidewall opposite the handle anchor and become visual reject points under gloss reflection. Liquid-contact pails for food are evaluated under FDA 21 CFR 177.1520(c) and Regulation (EU) No 10/2011; pails intended for UN-rated dangerous goods are pre-tested as UN 1H2 packagings with drop and stack conditioning at 40 °C for 28 days under ADR/RID/IMDG procedures where applicable. Compatibility limits apply to hydrocarbons above 50 °C, chlorinated solvents, and ketones; immersion screening under ASTM D543-20 and stress-crack testing under ASTM D1693-15 should be completed before filling. The terminal pails are 5-litre to 25-litre open-head containers for water-based paints, food ingredients, agricultural concentrates, and detergents.

    Comparative production-scale injection moulding process windows for Baystar HDPE 2287
    ApplicationMelt temperatureMould temperatureInjection velocityHold pressureCycle timeWall thickness
    Thin-wall dairy cups210–230 °C8–18 °C200–350 mm/s35–55 MPa4.5–7.0 s0.6–0.9 mm
    CSD closures220–240 °C8–15 °C250–400 mm/s40–60 MPa4.5–7.5 s0.9–1.2 mm
    Dairy and bakery crates210–240 °C15–25 °C90–150 mm/s50–70 MPa20–35 s2.5–5.0 mm
    Open-head pails220–250 °C12–20 °C120–180 mm/s45–60 MPa15–25 s1.8–2.5 mm
    Domestic storage articles210–230 °C10–20 °C150–250 mm/s35–50 MPa8–15 s1.2–2.0 mm
    Reusable industrial bins220–245 °C15–25 °C60–120 mm/s55–75 MPa30–50 s3.0–6.0 mm

    When a Domestic Storage Article is Injection Moulded from High-Flow HDPE Instead of Impact Copolymer PP

    When a 1-litre to 5-litre domestic storage box is converted from impact copolymer PP to Baystar HDPE 2287, the injection parameters shift because HDPE crystallizes more slowly and exhibits higher mould shrinkage anisotropy. Melt temperature is held at 210 °C to 230 °C, mould temperature at 10 °C to 20 °C, injection velocity at 150 mm/s to 250 mm/s, and hold pressure at 35 MPa to 50 MPa. For a 1.2 mm to 2.0 mm wall thickness, total cycle is 8 s to 15 s. The formulation includes 2 wt% to 4 wt% colour concentrate and, where improved stiffness and shorter cycle are desired, 0.5 wt% to 1.0 wt% of a nucleating masterbatch; nucleating addition above 1.0 wt% is not recommended in round bowls because out-of-round distortion can exceed 0.3 mm on a 150 mm diameter part. Food-storage versions must meet FDA 21 CFR 177.1520(c) and Regulation (EU) No 10/2011; articles intended for children’s use are additionally tested under EN 71-3:2019 for migration of eight elements and ASTM F963-17 for heavy metals. Dishwasher exposure above 70 °C can warp flat bases beyond 0.4% of the base dimension after repeated cycles; the grade is therefore positioned for ambient and refrigerated storage rather than high-temperature appliance service. The terminal products are stackable storage boxes, drawer organizers, and pantry bins whose snap-fit lids are produced in the same grade to avoid differential shrinkage.

    Reusable industrial bins and waste containers moulded from Baystar HDPE 2287 use wall sections from 3.0 mm to 6.0 mm and are processed on large injection machines with clamp forces from 8,000 kN to 20,000 kN. Melt temperature is 220 °C to 245 °C, mould temperature 15 °C to 25 °C, and injection velocity is kept at 60 mm/s to 120 mm/s to avoid flow marks on textured surfaces. Hold pressure of 55 MPa to 75 MPa with hold time 10 s to 20 s is required to prevent sink at thick rib intersections; total cycle is 30 s to 50 s. For waste containers exposed to outdoor UV, 2.0 wt% to 3.0 wt% carbon black masterbatch and 1.0 wt% to 2.0 wt% HALS masterbatch are added. Industrial bins used for non-food service must satisfy REACH and EU 2011/65/EU RoHS; when used in healthcare settings, surface cleanability is tested under ISO 22196:2011 for antibacterial activity only if an approved silver-based additive is compounded, but that additive is an optional downstream modification and is not part of the base resin certification. The critical process boundary is cooling uniformity in deep-draw tools: a core-to-cavity temperature differential above 5 °C produces taper distortion that binds the stacked bin. Published comparative data for this specific application are limited; mould trials should include short-shot series and pressure-drop studies on the first cavity. Terminal products are 50-litre to 120-litre reusable waste bins, hospital collection containers, and distribution totes.

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    Certification & Compliance
    More Introduction

    Bayport Polymers (Baystar) HDPE 2287 is a high-flow, high-density polyethylene injection-molding resin supplied in pellet form. Manufacturer literature lists a melt flow rate of 8.0 g/10 min at 190 °C/2.16 kg (ISO 1133-1:2022) and a density of 0.958 g/cm³ (ISO 1183-1:2019). The grade is specified for high-cavitation injection molding of thin-wall articles where shear-induced viscosity reduction during filling and a flexural modulus above 1,400 MPa (ISO 178:2019) are required. The narrow molecular weight distribution lowers recoverable strain and die swell in valve-gated hot-runner systems but limits extrusion blow molding parison stability.

    PropertyTest methodNominal value
    Melt flow rate, 190 °C/2.16 kgISO 1133-1:20228.0 g/10 min
    DensityISO 1183-1:20190.958 g/cm³
    Tensile stress at yield, 50 mm/minISO 527-2:201231 MPa
    Flexural modulus, 2 mm/minISO 178:20191,500 MPa
    Notched Charpy impact, 23 °CISO 179-1:20103.5 kJ/m²
    Vicat softening temperature, A50ISO 306:2022128 °C
    Heat deflection temperature, 0.45 MPaISO 75-2:201372 °C
    Mold shrinkage, parallelISO 294-4:20181.5%
    Mold shrinkage, perpendicularISO 294-4:20181.8%

    The property table lists nominal values, not sales specification limits. Lot-to-lot variation remains within manufacturer control limits, but exact compliance must be confirmed against the certificate of analysis for the intended production lot.

    Processing conditions. HDPE 2287 is not hygroscopic, but surface moisture can be introduced during outdoor silo storage or regrind transfer. When ambient relative humidity exceeds 60% or regrind content exceeds 20 wt%, desiccant drying at 70–80 °C for 1–2 h with a dew point of −20 °C or lower prevents splay. A conventional reciprocating screw with 20:1 L/D and compression ratio 2.5:1 is used for screw recovery. Barrel zone settings are 170–190 °C at the feed, 190–210 °C in transition, 210–230 °C in metering, and 230–240 °C at the nozzle. Melt temperature measured by an insertion pyrometer should remain between 210 °C and 240 °C. Drying should not exceed 80 °C to avoid pellet agglomeration and feed-bridging in the hopper throat.

    Processing parameterRecommended rangeEquipment basis
    Melt temperature210–240 °CPID-controlled reciprocating injection molding machine
    Mold temperature10–30 °CClosed-loop chilled water system
    Filling pressure80–120 MPaHydraulic injection unit
    Holding pressure50–80 MPaCavity-pressure transfer
    Back pressure2–5 MPaScrew recovery
    Screw speed80–120 rpm20:1 L/D general-purpose PE screw
    Drying70–80 °C for 1–2 h at dew point ≤ −20 °CDesiccant dryer

    Screw recovery speed is set so that plastication time remains shorter than cooling time but does not exceed 120 rpm. Screw speeds above 120 rpm raise melt temperature by shear heating and can force the melt above 240 °C, which reduces notched Charpy impact. Back pressure between 2 MPa and 5 MPa improves melt homogenization without extending cycle time. When switching from lower-viscosity resins, residual low-viscosity material causes screw slippage and uneven feed; purging with high-viscosity HDPE or a commercial purge compound for 15 min at 230 °C is required before production startup.

    When Cycle Time Reduction Governs Multi-Cavity Tool Performance

    Thin-wall packaging produced from HDPE 2287 is commonly molded at nominal wall sections from 0.7 mm to 1.2 mm. In a valve-gated hot-runner stack mold with 32 cavities, the controlling process response is pressure drop across the gate tip. Gates below 0.6 mm diameter create excessive shear heating and freeze before holding-pressure transfer, leaving insufficient packing compensation for volumetric shrinkage measured at 1.5% parallel and 1.8% perpendicular (ISO 294-4:2018). Gates above 1.2 mm diameter extend cycle time because gate solidification governs part ejection. For a 0.8 mm wall, a gate diameter between 0.7 mm and 1.0 mm is specified, with transfer from velocity control to pressure control at 95–99% filled volume. Holding pressure between 50 MPa and 80 MPa is applied until the gate freezes; failure to maintain this threshold results in sink marks and warpage.

    Cooling time scales with h²/(π² α), where h is wall thickness and α is thermal diffusivity approximately 8 × 10⁻⁸ m²/s. For a 0.8 mm wall, the conductive cooling characteristic time is 2.0 s, but ejection is delayed until the part surface reaches 80 °C or below to avoid post-mold distortion. Hot-runner heater profiling and insulated sprue bushings are required to hold the melt-temperature set point near 230 °C while preventing nozzle freeze-off at gate tips. Melt temperature above 250 °C accelerates oxidative chain scission; residence time greater than 5 min at this condition lowers viscosity and reduces notched Charpy impact (ISO 179-1:2010). Melt temperature below 200 °C raises filling pressure above the 120 MPa practical limit in thin-wall cavities, causing short shots or mold deflection. The practical melt-temperature window is therefore held between 210 °C and 240 °C, with a preferred set point of 230 °C for closure and pail configurations.

    In production-scale multi-cavity tools, cavity-pressure sensors with a sampling rate of 500 Hz are used to trigger the velocity-to-pressure transfer. Transfer by screw position alone produces cavity-to-cavity weight variation above 0.5%; transfer by cavity-pressure threshold at 90% of peak pressure reduces pack imbalance. Clamp force is selected from the projected area and the expected cavity pressure of 35 MPa during packing; a projected area of 300 cm² requires a clamp force of approximately 1,050 kN. Tools with less than 1,000 kN clamping capacity should not be used for thin-wall stack molds without finite-element validation of mold deflection.

    Twin-Screw Recompounding, Regrind Fraction, and Additive Limits

    Recompounding of HDPE 2287 with pigment or functional masterbatch is performed on a co-rotating twin-screw extruder with 40:1 L/D and side-feeder capability for mineral fillers. Because the base resin already carries a melt flow rate of 8.0 g/10 min (ISO 1133-1:2022), extended shear history produces molecular weight reduction and raises mold shrinkage anisotropy above the nominal values in ISO 294-4:2018. Regrind addition is limited to 30 wt% for thin-wall food packaging; higher regrind levels reduce notched Charpy impact and increase yellowing in unpigmented articles. When higher environmental stress-cracking resistance is required, the grade can be blended with a medium-molecular-weight HDPE, but melt flow rate decreases in proportion to the high-viscosity fraction.

    Avoid compounding with strong oxidizing masterbatches or lubricant packages containing metal stearates above 0.5 wt%; these additives plate out on mold vent surfaces and alter ejection friction. The base resin is supplied with a standard antioxidant package, but additional stabilization for prolonged hot-runner residence or outdoor exposure requires separate evaluation. Published data for high-filler-loading mechanical retention in this specific compound is limited; filler addition should be validated with tensile and impact testing under ISO 527-2:2012 and ISO 179-1:2010 before production-scale use.

    What Distinguishes Baystar HDPE 2287 from Broader-Specification Polyethylene Grades?

    Broader-specification HDPE grades for extrusion blow molding typically exhibit a melt flow rate below 1.0 g/10 min at 190 °C/2.16 kg (ISO 1133-1:2022) to preserve parison melt strength. HDPE 2287, with an MFR of 8.0 g/10 min, has insufficient parison melt strength for large bottle production; gravity-induced wall thinning occurs before mold closing. The same low melt elasticity is an advantage in injection molding because it suppresses die swell and improves replication of fine detail in tamper-evident closures. Against pipe-grade PE100 materials, the grade is not suitable for pressure pipe; PE100 requires a minimum required strength of 10 MPa at 20 °C for 50 years (ISO 9080:2012). The notched Charpy impact of 3.5 kJ/m² (ISO 179-1:2010) is lower than typical blow-molding HDPE values above 20 kJ/m², which restricts use in impact-dominated applications. The flexural modulus of 1,500 MPa (ISO 178:2019) is higher than the 1,100–1,300 MPa band for many blow-molding grades, providing stiffness for stacking pails and thin-wall containers. These distinctions position the product for injection-molded articles where processability, stiffness, and dimensional uniformity are primary, not for extrusion blow molding, pressure pipe, or thermoformed sheet.

    Food-contact suitability is assessed under FDA 21 CFR 177.1520(c) for olefin polymers and Commission Regulation (EU) No 10/2011 for plastic food-contact materials. Finished-article migration testing is conducted under EN 1186-1:2002 for overall migration and EN 13130-1:2004 for specific migration. In thin-wall dairy containers, the melt flow rate permits filling below 0.8 mm wall without exceeding the 120 MPa practical filling pressure; in closures, a gate diameter of 0.7 mm and mold temperature of 10–20 °C are used to maximize cycle time. For pails, the flexural modulus of 1,500 MPa (ISO 178:2019) contributes to stacking stiffness, but the grade is not selected where sub-zero drop impact is the sole design criterion. The resin is not intended for extrusion blow molding, high-pressure pipe, or continuous service above 100 °C.

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