Dow Hdpe Ng6997

Dow HDPE NG6997

    VTB
    Specifications
    HS Code 899057
    Density 0.954 g/cm³
    Melt Index 190 C 2 16 Kg 0.35 g/10 min
    Tensile Strength At Yield 27 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break 700%
    Flexural Modulus 1200 MPa
    Izod Impact Strength Notched 100 J/m
    Environmental Stress Crack Resistance Escr >1000 h
    Vicat Softening Temperature 125 °C
    Heat Deflection Temperature 70 °C
    Hardness Shore D 65
    Coefficient Of Linear Thermal Expansion 1.2E-4 /°C
    Water Absorption <0.01%
    Melting Point 130 °C
    Thermal Conductivity 0.45 W/m·K
    Volume Resistivity >1E16 ohm·cm
    Dielectric Constant 2.3
    Specific Heat 2.3 kJ/kg·K

    As an accredited Dow HDPE NG6997 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Dow HDPE NG6997 is typically packaged in 25 kg moisture-resistant bags, palletized for industrial shipping and handling.
    Container Loading (20′ FCL) Dow HDPE NG6997 polyethylene resin loaded in 20′ FCL; 25 kg bags, palletized, shrink-wrapped, securely stowed for ocean transport.
    Shipping Dow HDPE NG6997 is shipped as non-hazardous solid polyethylene pellets in bags, octabins, or bulk trucks/railcars. It is not regulated for transport under DOT, IMDG, or IATA. Store in a dry, cool area away from ignition sources. Use standard PPE and follow SDS handling guidance. Avoid prolonged skin contact.
    Storage Store Dow HDPE NG6997 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep original containers closed to prevent moisture and contamination. Avoid contact with strong oxidizing agents. Do not expose to prolonged UV. Stack pallets safely to prevent bag rupture. Use first-in, first-out inventory. Maintain good housekeeping to avoid pellet spills.
    Shelf Life Shelf life is typically two years from manufacture if stored cool, dry, and unopened in original packaging away from sunlight.
    Application of Dow HDPE NG6997

    Injection molding of thin-wall dairy and delicatessen containers from HDPE NG6997 on 32- to 64-cavity high-speed tools begins with validation of the resin's melt mass-flow rate under ISO 1133-1:2022 conditions at 190 °C / 2.16 kg because cavity fill below 0.45 mm wall stock depends on maintaining a consistent shear-viscosity profile. For food-contact formulations, the base resin is used at 100 wt% in single-material trays or at 70–85 wt% NG6997 with 15–30 wt% clean post-industrial in-house regrind generated from the same food-approved production line; post-consumer recycled HDPE is not added to thin-wall food-contact articles without a region-specific no-objection letter. Adding more than 30 wt% regrind is not advised for wall sections under 0.45 mm, because gate-area crystallinity inhomogeneity produces visible flow-line streaks and reduces top-load crush resistance measured on a universal testing machine at 50 mm/min. A colour or processing masterbatch is incorporated at 1–2 wt%, predispersed on a twin-screw extruder with an L/D ratio of 40:1 at 180–200 °C barrel set points to avoid unmelt agglomerates at the hot-runner valve pin. Compliance for this application is established under FDA 21 CFR 177.1520(c) 2.2 for high-density polyethylene in food contact and under EU Regulation 10/2011, with overall migration tested according to EN 1186-1:2002 and a limit of 10 mg/dm² in aqueous and fatty-food simulants. Molding lines should maintain melt temperature between 190 °C and 230 °C, mold surface temperature between 20 °C and 40 °C, injection velocity between 180 mm/s and 250 mm/s, and holding pressure between 40 MPa and 70 MPa; back pressure is held at 0.5–1.0 MPa with a screw cushion of 5–8 mm. Surface moisture on regrind exposed to storage at relative humidity above 60 % causes splay, so regrind is dried at 60–70 °C for 1–2 h before blending. Finished products include 150–500 mL dairy cups, 250–1000 mL deli tubs, 200–500 g margarine tubs, and frozen dessert containers with hinged lids that require more than 1 000 open-close actions without whitening on an in-house hinge cycling fixture.

    What Limits Torque Retention in 38 mm Water Bottle Closures Molded from High-Flow HDPE?

    Closure molding on high-cavitation cold-runner or valve-gated systems with HDPE NG6997 operates within a narrower viscosity window than thin-wall packaging because the tamper-evident band must not crack during bridge deformation yet must strip from the core without excessive reaming. Formulation for still-water and dairy closures uses 96.5–98.5 wt% NG6997, 1.5–3.0 wt% colour masterbatch, and 0.02–0.05 wt% erucamide slip additive; higher slip loadings above 500 ppm are not used because organoleptic migration into neutral water can exceed sensory threshold limits under EN 1622:2006 odour testing. For child-resistant and pharmaceutical closures, the resin formulation is restricted to 100 wt% virgin NG6997 with no recycled content, and compliance is documented against USP <661.1> and USP <661.2> plastic packaging physicochemical chapters. Production parameters include melt temperature 200–240 °C, mold temperature 10–25 °C, injection speed 80–160 mm/s, holding pressure 40–70 MPa, and clamp force between 1 800 kN and 3 500 kN for 32- to 64-cavity tools. Gate vestige on the top of the closure must remain at or below 0.25 mm to avoid sealing-surface interference; valve gates or sub-gates with sharp pin geometry are selected. Torque retention is measured on a digital torque stand with ±0.05 N·m accuracy, with acceptance limits between 1.5 N·m and 2.5 N·m for removal torque after accelerated aging. If mold temperature falls below 10 °C, residual skin orientation produces hinge whitening and torque retention drops below 1.2 N·m. Compliance for food-contact closures is established under FDA 21 CFR 177.1520(c) 2.2, EU Regulation 1935/2004, and EU 10/2011; personal-care closure configurations require additional REACH Annex XVII verification for skin-sensitizing substances in the colour masterbatch. Finished products include 38 mm bottled water closures, 30/25 mm sports caps, 42 mm dairy closure shells, and tamper-evident pharmaceutical closures.

    Downstream applicationNG6997 loading (wt%)Recycled/rework loading (wt%)Additive loading (wt%)Melt temperature (°C)Mold temperature (°C)
    Thin-wall food packaging100 or 70–8515–30 post-industrial regrind1–2 processing masterbatch190–23020–40
    Closures96.5–98.5; 100 for pharma01.5–3.0 colour; 0.02–0.05 erucamide200–24010–25
    Industrial pails90–100 depending UN classification0–10 for UN pails; 10–20 for non-hazardous0.3–0.8 UV or 2–4 antistat190–22010–25
    Returnable crates85–100up to 201–4 colour; 0.08–0.15 antioxidant; 0.2–0.6 UV200–23520–40
    Household storage95–1000–52–5 colour; 0.05–0.10 nucleant; 0.5–1.0 antistat195–22515–30
    Toys97–10001–3 colour190–22015–30

    UN 1H2 certification of open-top plastic pails molded from HDPE NG6997 imposes drop, stack, and hydraulic pressure tests that push sidewall geometry toward a minimum nominal wall of 1.8 mm, while the resin's high flow allows filling the sidewall-to-gate ratio without short shots on single-face tools with 4 000–8 000 kN clamp force. For hazardous-goods packaging, the formulation is limited to 100 wt% virgin NG6997 or 90–100 wt% virgin with not more than 10 wt% cleaned in-house regrind, because UN homologation results on environmental stress cracking and drop impact become unrepeatable above 10 wt% recycled content. Non-hazardous pails may use 10–20 wt% post-industrial regrind and 0.3–0.8 wt% UV stabilizer masterbatch for outdoor storage, while antistatic pails for solvent-free powder handling can incorporate 2–4 wt% antistatic masterbatch to target surface resistivity below 109 Ω/square measured under IEC 61340-2-3:2016. Resin compliance to ASTM D4976-12a for PE molding and extrusion materials is verified against the lot certificate. Manufacturing on 1.2–2.8 kg shot injection molding machines uses melt temperature 190–220 °C, mold temperature 10–25 °C, injection speed 40–80 mm/s for thick sections to prevent jetting, hold pressure 50–70 MPa, and cooling time 15–25 s; in-mold label inserts are held at 15–25 °C to prevent label sink migration. Drop compliance under UN 1H2 requires conditioning at -18 °C and stack testing at 40 °C for 28 days, so gate geometry is selected to avoid frozen-in notch stresses at the base rim. Finished products include 5 L, 10 L, 20 L, and 25 L open-top containers with tamper-evident tear tabs, lid gaskets, and compatibility with food, aqueous surfactant, and non-flammable chemical fill goods.

    When Returnable Pooled Crates Require ESCR After 2400 h Under ASTM D1693 Condition B

    Returnable pooled distribution crates molded from HDPE NG6997 are subject to repeated compression stacking, side-impact from conveyor lines, and outdoor UV exposure; the critical failure mode is environmental stress cracking at weld lines and gate bosses. Formulation for these thick-wall parts uses 85–100 wt% NG6997 with up to 20 wt% recycled HDPE whose melt mass-flow rate must be within ±20 % of the virgin lot's value under ISO 1133-1:2022, otherwise boss shrinkage at the moulded-in handle interlocks creates assembly interference. Colour masterbatch is added at 1–4 wt%, hindered phenolic antioxidant at 0.08–0.15 wt%, and ultraviolet stabilizer masterbatch at 0.2–0.6 wt% for crates stored outdoors more than 500 h per year. The production window on machines with 8 000–12 000 kN clamp force and 2.5–4.0 kg shots specifies melt temperatures 200–235 °C, mold temperatures 20–40 °C, holding pressure 35–60 MPa, and cooling times 18–35 s; sequential valve gating is used to push air traps away from the rim sealing surfaces. Weld-line performance is validated by ASTM D638-14 tensile bars cut perpendicular to the weld line and by ASTM D1693-15e1 environmental stress cracking using 10 % Igepal CO-630 solution at 50 °C; values should exceed 2400 h at Condition B before mold cooling channels are accepted. Compression set and top-load are tested under ASTM D642-20 at 23 °C and 50 % RH. Finished products include 30–65 L foldable distribution crates, nesting automotive spare-part boxes, bakery tray inserts, and reusable e-commerce totes that withstand 250 kg static top-load in a 5-high stack.

    ApplicationCompliance standard or regulationTest method or clauseLimit / condition
    Thin-wall food packagingFDA 21 CFR 177.1520(c) 2.2; EU 10/2011EN 1186-1:2002Overall migration 10 mg/dm²
    ClosuresFDA 21 CFR 177.1520(c) 2.2; EU 1935/2004; USP <661.1> / <661.2>EN 1622:2006; torque standRemoval torque 1.5–2.5 N·m
    Industrial pailsUN 1H2; ASTM D4976-12aIEC 61340-2-3:2016 if antistaticSurface resistivity below 109 Ω/square
    Returnable cratesASTM D1693-15e1; ASTM D638-14; ASTM D642-20ESCR, 10 % Igepal CO-630, 50 °C, Condition BESCR above 2400 h
    Household storageRoHS 2011/65/EU; REACH (EC) No 1907/2006; UL 94 HBIEC 61340-2-3:2016 if antistaticSVHC content below 0.1 wt%
    ToysEN 71-3:2019+A1:2021; ASTM F963-23; FDA 21 CFR 177.1520(c) 2.2; EU 10/2011Element migration; mechanical safetyOverall migration 10 mg/dm²

    In household storage articles and rigid appliance housings injection-molded from HDPE NG6997, multi-cavity cold-runner tools require direct melt-flow length through thin ribs to remain below 300:1 to avoid short-fill at the base of deep drawer walls. The formulation is 95–100 wt% virgin NG6997, with 2–5 wt% colour masterbatch when a consistent in-house colour library is required; if static dust attraction is a failure mode, 0.5–1.0 wt% antistatic masterbatch is used to reach surface resistivity below 1012 Ω/square, tested under IEC 61340-2-3:2016. Nucleating agent at 0.05–0.10 wt% is included when cycle-time reductions demand faster crystallization, but nucleated parts must be checked for impact loss at living-hinge corners using ASTM D256-23 notched Izod tests. Compliance for appliance housings follows RoHS 2011/65/EU restricted substance limits and REACH Regulation (EC) No 1907/2006 SVHC content below 0.1 wt%; flame classification is tested to UL 94 HB. Processing on machines with 1 200–2 500 kN clamp force uses melt temperature 195–225 °C, mold temperature 15–30 °C, injection velocity 120–200 mm/s, holding pressure 35–65 MPa, and cooling time 8–18 s depending on rib thickness. Draft angles below 0.5° on deep drawer sides cause ejection scuffing unless air-assisted ejection is used; textured mold surfaces require additional 1–2° draft to avoid wall deformation. Finished products include 15–120 L storage boxes, stackable drawer organizers, laundry baskets, and vacuum cleaner housing shells where dimensional stability after steam cleaning at 80 °C is required.

    When toy and child-contact articles are injection-molded from HDPE NG6997, formulation control starts with 97–100 wt% virgin resin and 1–3 wt% pigment masterbatch based on fully polymerised olefin carriers; no phthalate plasticisers, no polybrominated diphenyl ethers, and no heavy-metal pigments are permitted in this application. Migration of eight elements is evaluated under EN 71-3:2019+A1:2021, while mechanical safety for toys is tested under ASTM F963-23 for small parts, sharp edges, and bite-test dimensional retention. Food-contact mouth probabilities require the base resin to meet FDA 21 CFR 177.1520(c) 2.2 and EU 10/2011 with an overall migration limit of 10 mg/dm². Processing uses melt temperature 190–220 °C, mold temperature 15–30 °C, injection pressure 60–100 MPa, and screw back pressure 0.3–0.6 MPa to prevent local pigment separation at the gate blush zone. Mould release is achieved with non-silicating external release systems only where a food-contact listing is absent, because silicone migration alters paint adhesion on later decorating lines. Finished products include construction blocks, stacking toys, bath toy components, and rigid ride-on body parts. Published data for the specific interaction of post-consumer recycled HDPE with repeated dishwasher mouthing exposure in this exact product geometry is limited; therefore recycled content is not recommended for toys without application-specific migration clearance.

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    Certification & Compliance
    More Introduction

    Within the high-density polyethylene portfolio of the manufacturer, DOW HDPE NG6997 is identified as a fractional-melt extrusion blow-molding resin for monolayer and multilayer rigid packaging. The product designation carries no pre-blended colour; it is supplied as a natural resin that requires masterbatch addition when pigmented containers are specified. Density is reported as 0.957 g/cm³ under ASTM D1505. Melt flow rate is reported as 0.70 g/10 min at 190°C and 2.16 kg under ASTM D1238. Those two values place the grade in the intermediate-stiffness, fractional-melt segment of the density–flow matrix used for bottles and small-to-medium containers. The targeted property envelope includes high parison melt strength, resistance to environmental stress cracking, and sufficient tensile yield to allow down-gauging in high-speed bottle production. Published values for tensile yield strength, elongation at break, and flexural modulus are 28 MPa, 700%, and 1450 MPa, respectively, when tested under ASTM D638 and ASTM D790. Because the resin is specified for blow molding rather than injection molding or film extrusion, its molecular weight distribution and rheology are designed to maintain parison integrity at die gaps typical of continuous shuttle and reciprocating-blow machines.

    Processing trials on shuttle blow-molding equipment with 24:1 to 30:1 single-screw extruders indicate that melt-temperature control is more decisive than back pressure in controlling surface appearance and die swell. Melt temperatures between 175°C and 205°C are commonly used; temperatures above 210°C may produce odour, oxidation byproducts, and loss of parison melt strength. The melt is compatible with screw designs using a barrier section and Maddock mixing element, and screen packs of 20/40/60 mesh are adequate for unfilled natural resin. A desiccant hopper drying step at 80°C for 2 h to 4 h is warranted when incoming moisture exceeds 0.05% by weight or when storage relative humidity is above 60%.

    What Melt-Temperature, Die-Gap, and Blow-Pressure Settings Control Parison Stability?

    On intermittent shuttle blow molders, die gaps are typically set between 1.5 mm and 3.0 mm, with blow pressure of 0.6 MPa to 0.8 MPa and mold temperatures maintained between 10°C and 25°C. The grade’s fractional melt flow permits deep-draw handle pinch-off and controlled parison programming, but the die gap must be adjusted for container length-to-diameter ratio and target wall distribution. The following processing window is used as a starting point for monolayer containers on shuttle equipment.

    ParameterStarting rangeEquipment or method
    Melt temperature175–205°CMelt thermocouple at die entrance
    Die gap1.5–3.0 mmFeeler gauge at ambient die
    Blow pressure0.6–0.8 MPaMachine regulator at blow pin
    Mold temperature10–25°CCooling-water temperature at mold inlet
    Pre-drying80°C for 2–4 h if moisture > 0.05 wt%Desiccant hopper dryer
    Screen pack20/40/60 meshBreaker plate

    Deviations in melt temperature from the specified window are more consequential than in higher-flow grades because the high molecular weight distribution narrows the practical operating window. Low melt temperature increases melt fracture and uneven die swell; high melt temperature reduces sag resistance and can raise gel formation. When parison sag is observed, reduction of melt temperature to the lower half of the window is preferred over increasing blow pressure, because the latter can create thin spots at pinch-off.

    Environmental stress-cracking resistance is the primary differentiator in detergent, bleach, and agrochemical packaging. Under ASTM D1693 Condition A with 100% Igepal, the grade is positioned in the > 300 h class, although the exact public datasheet value can vary with specimen preparation and stress concentration. The ESCR margin permits the resin to be used with aggressive filled products without the immediate cracking observed in lower-molecular-weight general-purpose HDPE grades of similar density. For compatibility decisions, immersion testing under ASTM D543 is required for formulations containing strong oxidizers, aromatic solvents, or high-pH hypochlorite solutions. The resin is not recommended for continuous service above 60°C with strong oxidizers because oxidizing conditions accelerate chain scission and stress cracking.

    When DOW HDPE NG6997 Is Benchmarked Against Unimodal HDPE Blow-Molding Resins

    The practical difference is observable in parison stability and environmental stress-cracking resistance. A unimodal HDPE of similar density may provide equivalent short-term stiffness but lower resistance to environmental stress cracking under ASTM D1693; the molecular-weight distribution of DOW HDPE NG6997 is designed to maintain a higher tie-molecule population that delays crack initiation. In contrast, a bimodal pipe-grade HDPE offers higher slow crack growth resistance for pipe service but has a melt flow and shear viscosity unsuitable for bottle parison programming on shuttle blow-molding lines. The table below compares the typical property profile of DOW HDPE NG6997 against representative ranges for general-purpose unimodal blow-molding HDPE grades of the same nominal density class.

    PropertyDOW HDPE NG6997 typical valueUnimodal general-purpose HDPE class rangeTest method
    Density0.957 g/cm³0.955–0.960 g/cm³ASTM D1505
    Melt flow rate0.70 g/10 min0.30–0.80 g/10 minASTM D1238
    Tensile yield strength28 MPa24–29 MPaASTM D638
    Elongation at break700%600–800%ASTM D638
    Flexural modulus1450 MPa1100–1500 MPaASTM D790
    Environmental stress-cracking resistance> 300 h50–150 hASTM D1693
    Vicat softening point127°C120–128°CASTM D1525
    Shore D hardness6865–69ASTM D2240

    The principal difference is not density or short-term mechanical stiffness, but the failure time under ESC conditions. For a bottle containing a stress-cracking liquid such as a concentrated nonionic detergent, the higher tie-molecule fraction in HDPE NG6997 shifts failure from localized pin-hole cracking to more uniform stress relaxation. This has implications for wall thickness design: processors can reduce container mass in ESCR-limited applications when switching from a general-purpose grade, provided top-load and drop-impact requirements are independently satisfied under ASTM D2659 and ASTM D2463. The grade is not differentiated by transparency; it is a semi-crystalline HDPE with high light scattering, and applications requiring contact clarity should use a clarified polypropylene or a lower-density metallocene polyethylene instead.

    On high-output lines, the resin demonstrates stable parison length when run on continuous shuttle machines with 6 to 12 parison heads, provided the die temperature is controlled within ±3°C. Batch-to-batch variance in melt flow rate is monitored under ASTM D1238 with release limits typically around ±0.10 g/10 min; converters report that tooling changes are rare when switching lots. For multilayer containers, HDPE NG6997 is used as the skin layer with polyamide or EVOH barrier layers, but the high melt strength of the resin may require adjustment of adhesive tie-layer viscosity to maintain layer stability. No published oxygen transmission rate data for a specific bottle wall thickness are provided in the public datasheet; barrier calculations should be derived from measured bottle permeability using ASTM D3985 or ASTM F1307.

    Typical applications include bottles of 250 mL to 5 L for laundry detergents, household cleaners, bleach, automotive fluids, and certain pourable food containers. The material is selected when ESCR is controlling rather than optical clarity. It can be used in coextrusion blow molding with post-consumer recycled HDPE core layers, provided the PCR content is validated for layer thickness and final article impact performance under ASTM D2463. The fractional melt flow is not suitable for injection blow molding of thin-wall containers that require high-flow injection; for those applications, a higher-MFR HDPE injection grade should be selected.

    Regulatory Compliance and Incompatibility Boundaries

    Food-contact use requires confirmation against FDA 21 CFR §177.1520 olefin polymer requirements and, for EU applications, Commission Regulation (EU) No 10/2011 and its amendments. The manufacturer’s product stewardship summary should be consulted for migration limits, because finished-article compliance depends on layer structure, colorants, processing residuals, and surface-to-volume ratio. The resin is intended for single-use or limited-repeat-use packaging at ambient and moderate temperatures. It is not supplied with a UV stabilizer; outdoor service or prolonged ultraviolet exposure requires a separate UV masterbatch or carbon black compound. The grade should not be processed in equipment contaminated with polyvinyl chloride, acetal, or other thermally unstable resins that can generate acidic byproducts during melt processing. Avoid combination with amine-based additives unless pre-tested, because amine chemistry can reduce oxidative stability and affect organoleptic properties. High-shear processing above 210°C or extended residence times above 20 min should be avoided to limit gel formation and molecular-weight degradation. Electrical and electronic packaging applications may require assessment under RoHS Directive 2011/65/EU; the base resin contains no intentionally introduced lead, cadmium, mercury, hexavalent chromium, polybrominated biphenyls, or polybrominated diphenyl ethers.

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