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NOVAPOL LLDPE GI-2024-A

    • Product Name: NOVAPOL LLDPE GI-2024-A
    • 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 480303
    Density 0.924 g/cm³
    Melt Flow Index 24 g/10 min
    Tensile Strength At Yield 12 MPa
    Tensile Strength At Break 11 MPa
    Elongation At Break 580 %
    Flexural Modulus 350 MPa
    Shore Hardness D 53
    Izod Impact Strength Notched 5.0 kJ/m²
    Vicat Softening Temperature 80 °C
    Melting Point 124 °C
    Brittleness Temperature -70 °C
    Deflection Temperature Under Load 38 °C

    As an accredited NOVAPOL LLDPE GI-2024-A factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing NOVAPOL LLDPE GI-2024-A is supplied as free-flowing pellets in 25 kg bags, 500 kg sacks, or bulk quantities.
    Container Loading (20′ FCL) Container Loading (20′ FCL): NOVAPOL LLDPE GI-2024-A packed in 25-kg bags, palletized, and securely stowed in a 20-foot full container.
    Shipping NOVAPOL LLDPE GI-2024-A is a linear low-density polyethylene resin supplied as free-flowing pellets. It is non-hazardous, non-regulated for transport, and shipped in bulk bags, hopper trucks, or railcars. Keep dry, avoid excessive heat, and protect from contamination during transit.
    Storage Store NOVAPOL LLDPE GI-2024-A in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture pickup and contamination. Avoid prolonged storage above recommended temperatures. Ensure proper handling to minimize dust and static accumulation. Follow all safety data sheet guidelines.
    Shelf Life Shelf life is typically 12 months from manufacture when stored unopened in a cool, dry place away from direct sunlight.
    Application of NOVAPOL LLDPE GI-2024-A

    Processors targeting thin-wall injection-molded dairy packaging have used NOVAPOL LLDPE GI-2024-A as a primary matrix in multi-cavity stack molds at shot weights below 12 g and wall sections between 0.8 mm and 1.2 mm. The published nominal melt index of 20 g/10 min under ASTM D1238 at 190 °C/2.16 kg and nominal density of 0.924 g/cm³ under ASTM D1505 permit filling of flow length-to-thickness ratios in the range of 180:1 to 220:1 without exceeding injection pressure ceilings that trigger flash on valve-gated stack molds. Production-scale behavior on 150–300 t hydraulic toggle injection molding machines with screw L/D ratios of 20:1 to 24:1 indicates that the grade moves from a stable filling regime to a pressure-limited regime when the cavity wall drops below 0.6 mm. At that thickness, gate freeze time falls below 0.45 s, and the required filling pressure rises above 90 MPa, producing short shots in outer cavities and increasing cavity-to-cavity weight variance from ±0.3% to ±1.2% on a 32-cavity mold. The standard machine setpoints observed for dairy tub and lid applications are melt temperature 205–230 °C, mold temperature 15–30 °C, injection velocity 100–150 mm/s, holding pressure 35–55 MPa, hold time 2.5–5.0 s, and screw back pressure 0.5–1.0 MPa. For food-contact use, the grade is referenced against FDA 21 CFR 177.1520(c) olefin polymer provisions and Commission Regulation (EU) No 10/2011, with overall migration limited to 10 mg/dm² and specific migration limits governed by Annex I substances. The formulation is run at 100% virgin resin for full food-contact traceability, but short-run producers dry-blend 95–98 wt% GI-2024-A with 2–5 wt% of a nucleated LLDPE masterbatch to raise crystallization temperature; masterbatch addition above 5 wt% lowers the melt strength enough to generate gate blush and increases lot-to-lot gloss variation on ribbed container bases. Terminal products include dairy spread tubs, frozen dessert containers, thin-wall takeout lids, and stackable food storage inserts where cold-temperature impact resistance is required down to -20 °C. Pre-drying is not required when the resin is stored in sealed packaging below 60% relative humidity; if sacks are left open above 60% RH for more than 12 h, 2 h at 70 °C in a desiccant dryer prevents surface splay and reduces post-mold weight variation. The exact spiral flow curve for GI-2024-A is not consistently published across regional datasheets, so the above runout limit should be verified by mold-filling simulation rather than transferred from generic 20 g/10 min LLDPE data.

    Where Does GI-2024-A Fit in Injection-Molded Overcaps and Flexible Closures for Cold-Fill Beverages?

    Cold-fill beverage overcaps produced from NOVAPOL LLDPE GI-2024-A occupy a narrow design space in which the high melt index is used to reduce injection pressure in long, thin hinge sections, while the low density provides the flexibility required for repeated opening without hinge fracture. Processors running this grade in cold-runner sub-gated systems on 150–300 t machines report that a melt temperature of 210–240 °C, mold temperature of 15–30 °C, injection pressure of 60–85 MPa, and holding pressure of 40–60 MPa with a hold time of 3–7 s produce stable cap dimensions at wall thicknesses of 1.2–1.8 mm. The addition strategy for overcaps that must resist environmental stress cracking in dishwashing environments is typically 85–90 wt% GI-2024-A blended with 10–15 wt% high-density polyethylene having a density of 0.952–0.960 g/cm³; above 15 wt% HDPE, the low-temperature drop weight impact at -10 °C falls sharply and the closure can develop radial cracks at the tamper band under top-load application. Compliance for food-contact closures references FDA 21 CFR 177.1520(c) for olefin polymer closures, Regulation (EC) No 1935/2004 for general food-contact materials, and Commission Regulation (EU) No 10/2011 for plastic materials and articles intended to come into contact with food. If the closure is used on non-food personal-care packages, the relevant framework is REACH Regulation (EC) No 1907/2006 and, where applicable, Directive 2011/65/EU RoHS for electrical cosmetic devices. The grade is not recommended for hot-fill systems above 85 °C because the low-density backbone loses sealing force through stress relaxation faster than HDPE closure resins; published data on cyclic compression set under hot-fill conditions for this specific GI-2024-A configuration is limited, so closure torque decay on a given bottle finish should be validated by torque-retention testing rather than inferred from short-term density measurements. Terminal products include sports drink overcaps, flip-top closures for personal-care bottles, tamper-evident hoods, and flexible child-resistant outer caps where the polymer contributes a softer touch than HDPE without full elastomer modification.

    Housewares Molding: Dimensional Stability and Warpage Control

    Multi-cavity housewares tooling places a premium on uniform fill speed rather than absolute melt-index elevation. In this application, NOVAPOL LLDPE GI-2024-A is run at 100% for simple pantry bins and drawer organizers, while cold-storage containers are reformulated at 90–95 wt% GI-2024-A with 5–10 wt% low-density polyethylene to raise impact toughness at -25 °C; LDPE addition above 10 wt% reduces flexural modulus below 250 MPa and produces sink marks at rib intersections deeper than 0.15 mm. The downstream process uses reciprocating-screw injection molding machines with clamp force from 400–900 t, melt temperature 190–230 °C, mold temperature 20–35 °C, injection pressure 70–110 MPa, and a stepped packing profile of 75 MPa, 50 MPa, and 25 MPa over 4–8 s. A cushion of 4–8 mm is maintained to prevent screw bottoming and to stabilize the pressure transfer into thick rounded corners, where housewares parts typically exhibit shrinkage-induced voids if the hold pressure decays too early. The relevant compliance framework for kitchen and food-storage housewares is FDA 21 CFR 177.1520(c) for olefin food-contact articles, Commission Regulation (EU) No 10/2011 for EU-bound articles, and REACH Regulation (EC) No 1907/2006 for broader chemical registration. For general non-food housewares, mechanical performance is assessed against ASTM D638-14 for tensile flow, ASTM D790 for flexural modulus, and ASTM D256 or ISO 179-1 for notched impact depending on the buyer’s specification. A common failure mode on warehouse racks is warpage of stackable lids after demolding, which is controlled by balanced cooling circuits in the core and cavity rather than by increasing packing pressure alone; differential mold temperature beyond 5 °C between core and cavity has been observed to produce corner lift exceeding 1 mm on 400 mm long bins. Terminal products include stackable storage totes, waste bins, kitchen drawer organizers, under-bed cases, and freezer-safe lidded boxes.

    Application boundaryGoverning standard or regulatory instrumentTypical addition strategyRepresentative process windowTerminal product type
    Thin-wall dairy packagingFDA 21 CFR 177.1520(c); Commission Regulation (EU) No 10/2011100% virgin or 95–98 wt% GI-2024-A with 2–5 wt% nucleated LLDPE masterbatchMelt 205–230 °C; mold 15–30 °C; hold 35–55 MPaDairy tubs, frozen dessert containers, takeout lids
    Cold-fill closures and overcapsFDA 21 CFR 177.1520(c); Regulation (EC) No 1935/2004; EU No 10/201185–90 wt% GI-2024-A with 10–15 wt% HDPEMelt 210–240 °C; mold 15–30 °C; hold 40–60 MPaBeverage overcaps, flip-top closures, tamper-evident hoods
    Housewares and cold-storage articlesFDA 21 CFR 177.1520(c); REACH Regulation (EC) No 1907/2006; ASTM D638-14100% or 90–95 wt% GI-2024-A with 5–10 wt% LDPEMelt 190–230 °C; mold 20–35 °C; stepped pack 75/50/25 MPaStorage totes, bins, drawer organizers, freezer boxes
    Laboratory and diagnostic disposablesISO 13485:2016; REACH Regulation (EC) No 1907/2006; FDA 21 CFR 177.1520(c) where applicable100% GI-2024-A or 90–95 wt% GI-2024-A with 5–10 wt% HDPE for gamma-stable traysMelt 200–225 °C; mold 10–25 °C; hold 40–60 MPaPipette tip racks, microtube racks, diagnostic cartridge housings
    Agricultural irrigation fittingsREACH Regulation (EC) No 1907/2006; RoHS Directive 2011/65/EU; ISO 527-2; ISO 179-170–85 wt% GI-2024-A with 15–30 wt% HDPEMelt 200–240 °C; mold 15–40 °C; hold 50–70 MPaDrip emitter bodies, barbed connectors, stake fittings
    Industrial pail lids and hinged closuresASTM D1693-15; ASTM D638-14; ISO 179-190–95 wt% GI-2024-A with 5–10 wt% HDPEMelt 210–235 °C; mold 20–30 °C; hold 45–60 MPaPail lids, screw caps, flexible hinge lids for household chemicals

    For non-sterile laboratory disposables and in-vitro diagnostic housing components, Grade GI-2024-A is selected less for its tensile properties than for its clean feedstock consistency and low additive package. Cleanroom injection molders running 100% GI-2024-A on polished A2 tool steel with clamp force from 80–180 t use melt temperatures of 200–225 °C, mold temperatures of 10–25 °C, injection velocities of 80–130 mm/s, and holding pressures of 40–60 MPa to fill thin channels in pipette tip racks without flash at ejector pin clearances below 0.02 mm. For gamma-stable diagnostic trays, the formulation shifts to 90–95 wt% GI-2024-A with 5–10 wt% high-density polyethylene to improve resistance to post-irradiation embrittlement; higher HDPE loadings above 10 wt% reduce the dimensional accuracy of interlocking well plates and can increase warpage after 25 kGy gamma exposure. Molders should avoid peroxide or amine-based release modifications because these additives elevate the post-irradiation carbonyl index and create discoloration in translucent parts without a compensating antioxidant package. The applicable quality framework is ISO 13485:2016 for manufacture of components supplied to diagnostic and medical device assemblers, while material compliance is verified against REACH Regulation (EC) No 1907/2006 and, for food-contact sample collection accessories, FDA 21 CFR 177.1520(c). If the molded part is not intended to be patient-contacting, full ISO 10993-1 biocompatibility evaluation is not required, but the processor must nevertheless document that no animal-derived additives or phthalate plasticizers are introduced during handling, regrind control, or packaging. Storage above 60% relative humidity in cleanroom staging areas has been observed to produce surface splay and microbiological packaging moisture; pre-drying at 70 °C for 2 h is implemented before molding when bags have been opened beyond 8 h. Terminal products include pipette tip racks, microtube racks, diagnostic cartridge housings, and secondary container components for sample transfer kits.

    When Low-Temperature Ductility Governs Agricultural Fitting Performance

    In low-pressure irrigation networks, the dimensional stability of barbed fittings at sub-zero ambient conditions becomes the controlling material criterion. GI-2024-A is used at 70–85 wt% with 15–30 wt% high-density polyethylene to raise the tensile modulus into the 450–600 MPa range while retaining enough elongational flexibility to snap onto low-density polyethylene tubing without barb-root cracking. Above 30 wt% HDPE, the elongation at break under ISO 527-2 falls below 400%, and the fittings begin to show brittle fracture at -10 °C when pulled off a mating spike at an angle greater than 15°. The production process for these small, thick-walled fittings uses 100–250 t injection molding machines with cold-runner multi-cavity tools, melt temperature 200–240 °C, mold temperature 15–40 °C, injection velocity 60–100 mm/s, and holding pressure 50–70 MPa for 5–10 s. Leakage-path cross-sections below 0.4 mm in emitter bodies require intensified packing because the thin land freezes early, and insufficient hold pressure creates micro-leak channels that only appear under 200 kPa network pressure after thermal cycling. Mechanical acceptance tests are commonly conducted under ISO 527-2, ISO 179-1, and ISO 178, while material compliance is verified against REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU for electrical or automated irrigation controls. The grade is not formulated as a potable-water pressure-pipe resin, so it should not be specified as the primary pressure boundary component in municipal water distribution; its appropriate boundary is low-pressure agricultural drip and micro-irrigation fitting bodies where the fluid is non-potable or the fitting is downstream of a pressure regulator. Terminal products include drip emitter bodies, barbed connectors, stake fittings, micro-sprinkler bases, and valve bodies for 12–20 mm LDPE laterals.

    Industrial Container Lids Must Balance ESCR Against Hinge Fatigue

    Injection-molded lids for 20–30 L industrial pails fail most often not by burst pressure but by environmental stress cracking at the hinge root when the closure is opened at ambient temperatures below 5 °C. For such lids, GI-2024-A is compounded at 90–95 wt% with 5–10 wt% high-density polyethylene; this addition level improves stress-crack resistance under ASTM D1693-15 condition B in 100% Igepal CO-630 while retaining the low-temperature hinge ductility expected of an LLDPE-rich matrix. Increasing HDPE above 10 wt% raises the hinge whitening rate after 5,000 repeated open-close cycles and produces audible hinge-root cracking before 10,000 cycles in unmodified tools. The downstream process uses two-plate cold-runner or valve-gated tools on 250–500 t machines, with melt temperature 210–235 °C, mold temperature 20–30 °C, injection pressure 60–90 MPa, and pack/hold pressure 45–60 MPa applied for 0.8–1.5 s/mm of wall thickness. Cooling time is set between 4–8 s depending on lid thickness; demolding with a three-stage ejection profile and post-mold cooling fixtures controls ovality below 1.0 mm on a 400 mm diameter lid. The applicable mechanical verification set includes ASTM D638-14 for tensile properties, ASTM D1693-15 for environmental stress-crack resistance, and ISO 179-1 for notched impact; chemical-compliance documentation for export may also require REACH Regulation (EC) No 1907/2006 and, for food-packaging pails, FDA 21 CFR 177.1520(c) or Commission Regulation (EU) No 10/2011. Published data for long-term hinge-retention behavior of this specific grade under repeated torsional loading is limited, so hinge designs with a minimum notch root radius of 0.5 mm and a maximum opening angle of 135° are used by converters to stay within the known ductility envelope. Terminal products include injection-molded lids for industrial pails, screw caps for 20–30 L containers, and flexible hinge lids for bulk household chemical packaging.

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    Certification & Compliance
    More Introduction

    NOVAPOL LLDPE GI-2024-A is a linear low-density polyethylene resin configured for injection molding rather than for blown film or cast film conversion. The model designation encodes its injection-grade positioning: a nominal melt index of 20 g/10 min measured at 190 °C under 2.16 kg load in accordance with ASTM D1238 and ISO 1133-1:2022, and a nominal density of 0.924 g/cm³ determined by ASTM D1505. The resin is differentiated from standard Novapol LLDPE film grades by its high melt flow and from HDPE injection grades by its lower density and modified balance of stiffness and environmental stress crack resistance.

    Thin-wall food containers, disposable lids, overcaps, pails, housewares and non-pressure closures represent the principal conversion routes for this material. The high melt index reduces pressure loss in multicavity tools and permits filling of wall stock below 0.8 mm when gate size and venting are correctly proportioned. However, published spiral-flow data for this specific grade is limited; mold-filling analysis should use material data from a validated rheology dataset rather than generic high-flow LLDPE values. The resin is not intended for pressure pipe, blown film, or extrusion blow molding, where lower melt flow indices are required for melt strength and parison stability.

    Because the density is 0.924 g/cm³, the resin sits between low-density polyethylene and high-density polyethylene in crystallinity. The lower crystallinity, relative to HDPE, contributes to reduced shrinkage anisotropy and lower warpage in flat parts, but it also lowers heat resistance and top-load stiffness. The product should not be selected for continuous service above 60–65 °C unless specific load and duration data are generated according to ISO 75-2 or ASTM D648.

    What Rheological Response Is Obtained at 190 °C and 2.16 kg?

    The melt mass-flow rate of 20 g/10 min under 2.16 kg load indicates a low-viscosity polyethylene, but melt flow rate alone does not describe injection shear response. The polymer class is linear low-density polyethylene; molecular architecture is predominantly linear with short-chain branches introduced through comonomer addition. In practice, the material exhibits less shear thinning than high-pressure LDPE of similar melt index. Consequently, mold-filling simulations based solely on melt index understate pressure requirements in narrow gates at high shear rates. Capillary rheometry data at 190 °C and shear rates between 10 s⁻¹ and 1,000 s⁻¹ should be used to fit Cross-WLF or Carreau-Winter parameters, not single-point viscosity approximations.

    High flow at moderate molecular weight generally shortens cycle time because lower melt viscosity permits lower injection pressure and shorter hold-pressure time. However, high flow also lowers melt strength. In hot-runner systems, drool at valve gates can occur if melt temperature exceeds 230 °C or barrel residence time exceeds 5 minutes. These operational boundaries are derived from general polyethylene processing practice; published data specific to GI-2024-A is limited.

    Multicavity closure molds with 16 to 64 cavities and cold sprue bushings require a residence-time audit of the barrel volume against shot weight. When shot weight falls below 30% of barrel capacity, melt residence time rises and the possibility of oxidation-discoloration streaks increases. On production-scale toggle-clamp machines in the 1,200–1,800 kN range, processors have used nozzle melt temperatures of 180–210 °C for thick lids and 210–230 °C for thin-wall containers, with mold-coolant temperatures of 10–25 °C for fast freezing and 30–50 °C when dimensional tolerance is more critical. The exact temperature profile must balance short-shot risk against warpage and gate-stringing; there is no single universal setpoint because cooling geometry, hot-runner balance, and gate type dominate.

    Gate blush and jetting are the two most frequently reported surface defects when injection velocity is improperly configured. In thin-wall parts, jetting occurs when the melt stream enters the cavity without establishing a filling front against the cold mold wall; a slight reduction in injection velocity or a move to a tab gate typically resolves the defect. In contrast, gate blush around pinpoint gates indicates excessive shear heating. Melt temperature measured at the nozzle can remain within setpoint while local melt temperature in the gate rises above 240 °C, producing streaking or yellowing. Molders are advised to monitor nozzle pressure curves and gate geometry rather than relying solely on barrel setpoints.

    Shrinkage of high-flow LLDPE is nonisotropic. Flow-direction shrinkage may differ from transverse-direction shrinkage by 0.2–0.5 percentage points depending on gate location and packing time. Precision lids should be qualified by measuring molded parts after 24 h and 48 h at 23 °C ± 2 °C and 50% ± 5% relative humidity per ISO 294-4. Preconditioning at 40 °C accelerates post-crystallization, but it can overstate final shrinkage for parts used at ambient temperature.

    Weld-line strength in complex multicavity tools is influenced by melt temperature and packing pressure. Because high-flow grades have lower melt viscosity, they can penetrate melt fronts more readily, but venting and knit-line formation still require unobstructed flow paths. Any assessment of weld-line strength should follow ASTM D638 on machined or molded specimens taken across the weld line, not the base material values.

    Post-industrial regrind from sprues and runners can be reincorporated at controlled levels, provided the regrind is free of contamination and has not suffered oxidative degradation. Melt flow can increase with repeated processing due to chain scission, so the melt index of regrind should be measured after each pass. A common boundary is to maintain regrind ratio at no more than 30% by weight unless process capability studies show acceptable lot-to-lot variation.

    Melt Processing Parameters and Machine Boundary Conditions

    The following processing ranges are indicative of production practice for high-flow LLDPE injection grades. The values are not a replacement for machine-specific optimization; cycle time, clamp force, and gate freeze time should be established with a design of experiments using the actual mold and machine.

    Barrel temperature profiles typically progress from 160–180 °C in the feed zone to 180–210 °C in the compression zone and 190–220 °C in the metering zone. Nozzle melt temperature should be maintained at 180–230 °C, depending on wall thickness and hot-runner design. Mold temperatures between 10 °C and 50 °C are common; lower mold temperatures reduce cycle time, while higher mold temperatures reduce flow-induced stress and improve flatness. Transfer injection pressure should be recorded as cavity pressure rather than hydraulic pressure, with typical cavity pressures at transfer between 35 MPa and 60 MPa for easy-flow polyolefins. Hold pressure should be 50–80% of transfer pressure, and gate freeze must be verified by part weight stability rather than timer alone. Back pressure should be limited to 0.5–1.5 MPa hydraulic and screw speed to 50–150 rpm to avoid excessive shear heating.

    Pre-drying is not typically required for polyethylene. If storage conditions have produced surface condensation on cold pellets, hopper drying at 80 °C for 1–2 h may be used. Avoid blending with polypropylene, ethylene-vinyl alcohol, or ionomer residues in the same feed stream unless the entire regrind stream has been audited; such blends alter die swell, melt strength, and chemical resistance.

    ParameterNominal valueUnitTest method
    Melt mass-flow rate20g/10 minASTM D1238 / ISO 1133-1:2022
    Density0.924g/cm³ASTM D1505 / ISO 1183-1

    Additional mechanical properties such as tensile yield, elongation, flexural modulus, and impact are lot-specific. They are reported in the manufacturer certificate of analysis and should be measured on molded plaques or parts according to ASTM D638, ASTM D790, and ASTM D256 or their ISO equivalents. Published generic data for high-flow LLDPE cannot replace lot-specific results for critical part qualification.

    Crystallization behavior of LLDPE at this density is cooling-rate dependent. Slow cooling increases crystallinity and mold shrinkage, while rapid cooling reduces crystallinity and improves impact at the expense of modulus. Because injection molding is a fast-cooling process, mechanical properties measured on compression-molded plaques under slow cooling can deviate from those of molded parts. This is one reason why ASTM D638 and ASTM D790 values from generic datasheets are not direct predictors of as-molded part performance.

    When High-Flow LLDPE Replaces HDPE in Lightweight Closures

    Substitution of HDPE with GI-2024-A is considered when downgauging and impact resistance are more important than top-load stiffness. HDPE of similar melt index and density 0.952 g/cm³ offers higher flexural modulus and heat deflection temperature, but a lower environmental stress crack resistance under certain detergents and surfactants. The LLDPE density of 0.924 g/cm³ reduces part weight and generally improves low-temperature impact. However, the same density reduction lowers yield strength and can increase cycle time if mold cooling is not adjusted. Published data for this specific grade in such substitution trials is limited; comparative testing under ASTM D256 or ISO 179-1 for impact, and ASTM D790 or ISO 178 for flexural modulus, should be performed with the actual part geometry.

    Against standard blown-film LLDPE grades with melt indices between 0.5 g/10 min and 2.0 g/10 min, GI-2024-A has a much lower melt viscosity, which shifts its utility from film bubble stability to injection mold filling. It is not recommended for blown film; a melt index of 20 g/10 min reduces bubble stability under typical blow-up ratios above 2.0:1. Similarly, the grade is not a drop-in for high-pressure LDPE in extrusion coating or for HDPE in blow molding, because high melt flow reduces melt strength and die/parison control.

    Differentiating parameterNOVAPOL LLDPE GI-2024-ATypical HDPE injection gradeTypical LLDPE blown film grade
    Melt index at 190 °C/2.16 kg20 g/10 min20 g/10 min class0.5–2.0 g/10 min
    Density0.924 g/cm³0.952 g/cm³0.918 g/cm³
    Primary conversion routeInjection moldingInjection moldingBlown/cast film
    Processing consequenceLong flow length in thin walls; reduced warpage tendencyHigher top-load stiffness and heat resistanceBubble stability; high melt strength

    Regulatory use of this resin in food-contact applications must be confirmed through the current NOVA Chemicals product stewardship bulletin. Polyethylene grades in the Novapol family may be manufactured to meet FDA 21 CFR 177.1520 and EU Regulation 10/2011; however, a grade-specific letter of assurance should be obtained for each production lot. The resin is not intended for medical implant use. Under REACH 1907/2006 and RoHS 2011/65/EU, this polyethylene grade is not expected to contain regulated metals, PBB, or PBDE at reportable thresholds, but exact compliance documentation is a supplier-specific matter. Applications requiring UL flammability ratings or railway smoke-density standards require separate compound evaluation.

    High-cavitation closure tools with hot-runner systems benefit most when the material is run at the lower end of the melt temperature range and with short residence time. The performance boundary is not the melt index alone; it is the combination of cavity filling, gate freeze, part ejection, and cooling. Molds with insufficient venting cannot use the high flow to full advantage because gas compression at the end of fill creates short shots and burn marks even when pressure is adequate. Tooling should maintain vent depths below 0.02 mm for polyolefins and balance runner lengths across cavities. In such production environments, the main difference from previous-generation LLDPE grades is the predictable lower viscosity and the reduced need to increase melt temperature, which shortens recovery time and lowers thermal degradation risk.

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