| HS Code | 501203 |
| Density | 0.950 g/cm3 |
| Melt Mass Flow Rate 190 C 2 16 Kg | 7.5 g/10 min |
| Tensile Strength At Yield | 25.0 MPa |
| Tensile Strength At Break | 20.0 MPa |
| Tensile Elongation At Break | 1000 % |
| Flexural Modulus | 1100 MPa |
| Notched Izod Impact Strength 23 C | 80 J/m |
| Vicat Softening Temperature | 127 °C |
| Deflection Temperature Under Load 0 45 Mpa | 73 °C |
| Shore D Hardness | 66 |
| Mold Shrinkage | 1.5-3.0 % |
| Water Absorption | <0.01 % |
| Thermal Conductivity | 0.44 W/m·K |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 /°C |
| Volume Resistivity | >1.0E15 ohm·cm |
| Dielectric Constant 1 Mhz | 2.3 |
As an accredited Dow HDPE DMDB-7950 NT 7 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically, Dow HDPE DMDB-7950 NT 7 comes in 25 kg polyethylene-lined paper bags, stacked on pallets for industrial handling. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Dow HDPE DMDB-7950 NT 7, 25 kg bags, palletized, 880 bags, 22 MT net. |
| Shipping | Dow HDPE DMDB-7950 NT 7 is a non-hazardous polyethylene resin. It is typically shipped in 25 kg bags on pallets, octabins, or bulk trucks/railcars. Not classified as dangerous goods; no special transport placards required. Store dry, away from heat, moisture, and contamination, per SDS. |
| Storage | Store Dow HDPE DMDB-7950 NT 7 indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and open flames. Keep original bags or containers sealed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure, excessive stacking, and temperature extremes. Store away from strong oxidizers. Follow the manufacturer’s SDS, label instructions, and local storage regulations. |
| Shelf Life | Shelf life is 24 months from manufacture when stored in original, unopened packaging, protected from direct sunlight and moisture. |
For monolayer extrusion blow molding of UN 1H1 open-head and tight-head drums from 25 L to 120 L, Dow HDPE DMDB-7950 NT 7 is processed on accumulator-head machines with shot capacities of 8 kg to 30 kg. The extruder should use a barrier-screw design with 24:1 to 30:1 L/D ratio and a Maddock mixing section; screen packs are normally 20/60/20 mesh. Melt temperature at the die remains between 190 °C and 210 °C. Die gap is held at 1.8 mm to 2.5 mm, with die land length 20 mm to 30 mm to stabilise parison swell. Blow ratio is 2.4:1 to 2.8:1. Pre-blow pressure ranges from 0.10 MPa to 0.30 MPa; high-pressure blow air is 0.6 MPa to 0.8 MPa. Mold temperature is controlled at 12 °C to 25 °C. Up to 20 wt% clean in-house regrind can be reintroduced at the feed throat if it is ground to 5–10 mm flake, passed through a 60 mesh screen pack, and kept free of paper labels and silicate dust. If the resin is stored at relative humidity above 60%, drying at 80 °C for 2 h in a dehumidifying hopper prevents surface splay at the die lip. The grade is not an injection-molding resin; the low melt flow rate restricts spiral flow length below the threshold for thin-wall caps or closures. The nominal datasheet values are density 0.951 g/cm³ per ISO 1183-1:2019 and melt flow rate 0.07 g/10 min per ISO 1133-1:2022. Environmental stress-cracking resistance of the material exceeds 1000 h under ASTM D1693 Condition A at 50 °C in 100% Igepal CO-630, supporting service with petroleum lubricants, detergents, and water-based chemicals. The packagings are tested under the UN Model Regulations Chapter 6.1, including stacking test 6.1.5.6, drop test 6.1.5.3, and leakproofness test 6.1.5.4. For food contact, the olefin polymer is listed under FDA 21 CFR 177.1520 when used in monolayer construction. The terminal products are 25 L jerrycans, 60 L open-head drums, and 120 L tight-head drums for dangerous goods and non-dangerous industrial liquids.
Top shoulder thinning, not base rupture, is the dominant failure mode in 1000 L intermediate bulk container inner bottles. The shot size for this application is 9 kg to 12 kg, and accumulator-head capacity should exceed the maximum shot weight by at least 15% to avoid hesitation lines at the parison surface. Extruder diameter is 120 mm to 150 mm with a 30:1 L/D ratio. Melt temperature must remain at the lower boundary of 185 °C to 200 °C to preserve zero-shear viscosity and limit parison draw-down. Die gap is set at 2.2 mm to 2.6 mm, and die land length is 30 mm to 40 mm for melt relaxation before exit. A parison programming curve with 30–35% thickness reduction at the top region and 10–15% reduction at pinch-off prevents excessive flash and maintains minimum wall thickness above 1.8 mm in the finished bottle. For outdoor chemical service, 2.0–3.0 wt% carbon black masterbatch is added; the resulting UV-stabilised bottle is used for alcohol, glycol, and non-oxidising acid transport. Published data for exact parison sag rate under production thermal conditions is limited, but the resin’s low melt flow is selected specifically to hold parison geometry over the long draw length required for 1000 L inner bottles. The bottle is certified as UN 31H1 for liquid dangerous goods under ADR, RID, and the IMDG Code. Terminal products are 1000 L IBC inner containers for industrial liquid transport and storage.
Agricultural chemical packaging imposes simultaneous environmental stress-cracking resistance and permeation constraints that linear low-density grades fail at wall thicknesses below 1.5 mm. DMDB-7950 NT 7 is used as the structural outer layer and regrind carrier in six-layer coextrusion blow molding. A typical layer distribution is 40 wt% outer HDPE, 30 wt% regrind, 5 wt% maleic anhydride grafted polyethylene tie layer, 5 wt% EVOH barrier with 38 mol% ethylene content, 5 wt% tie layer, and 15 wt% inner HDPE. Inline fluorination uses 0.1–0.5 vol% fluorine in nitrogen during blowing; treatment time is 10 s to 30 s. The resulting fluorinated inner surface is 50 nm to 100 nm thick and reduces permeation of xylene, cyclohexanone, and ester-based solvents. Fluorination units require continuous emission abatement and process gas monitoring because free fluorine is a strong oxidiser. The terminal containers are 1 L, 5 L, and 20 L narrow-neck bottles for emulsifiable concentrates, suspension concentrates, and oil dispersions used in crop protection. Packaging compliance follows UN 1H1 dangerous goods requirements, FAO/WHO guidelines for pesticide storage, and EU CLP labelling. The regenerated inner layer is not used in contact with volatile solvents beyond the validated barrier structure because pinholes in the fluorinated layer become primary failure sites.
To achieve insert retention around pump grommets, three-dimensional parison control is coupled with chill-mold temperatures from 8 °C to 15 °C. Wall thickness is held at 2.0 mm to 3.0 mm for reservoirs with volumes from 1.5 L to 5.0 L. Pinch weld thickness should not fall below 1.8 mm, and the pinch zone is trimmed to a residual flash height of less than 0.5 mm. Mold shrinkage is 1.5–2.5% after 24 h at 23 °C and 50% relative humidity, measured per ISO 294-4. Heat aging at 90 °C for 24 h per ISO 188 should not produce visible distortion or grommet loosening. Continuous service temperature is limited to 60 °C, and continuous system pressure must remain below 0.3 bar; the material is not specified for pressurised coolant expansion vessels. Compliance is maintained under IATF 16949:2016 with PPAP level 3 submissions and OEM-specific washer fluid compatibility validation. Terminal products are windshield washer reservoirs and coolant overflow bottles for light commercial vehicles and passenger cars.
Cold-conditioned drop testing of 200 L tight-head drums at -18 °C exposes pinch-weld stress concentrations that are invisible at 23 °C. UN Model Regulations 6.1.5.3 requires conditioning for 24 h at -18 °C; for packing group II liquids, drop height is 1.2 m. Mold temperature should be held at 15 °C to 20 °C, and drums require 48 h post-mold stabilisation at 20 °C and 50% relative humidity before conditioning. Wall thickness distribution is set at 4.0–4.5 mm in the bottom chimb area, 2.8–3.2 mm in the body, and 3.5–4.0 mm at the upper shoulder. Parison programming reduces top neck thickness by 40% to prevent fold-over and stress concentration at the closure. The pinch weld is trimmed below 1.0 mm residual flash because thick pinch remnants act as crack-initiation sites under cold impact. Notched impact and ASTM D1693 slow-crack-growth data do not fully predict cold drop failure; instrumented impact tensile evaluation under ISO 8256 gives better correlation with pinch-weld brittleness. Terminal product is the 200 L tight-head drum for liquid dangerous goods, including oxidising liquids and corrosives, where low-temperature drop performance is part of UN type approval.
Potable water contact applications require extraction and organoleptic limits that are separate from mechanical performance. DMDB-7950 NT 7 is suitable for extrusion blow molded water softener brine tanks from 100 L to 300 L and non-pressurised filter housings. The contact layer is produced from 100% virgin resin with no external lubricants or slip agents. Melt temperature is held at 190 °C to 210 °C, and residence time in the accumulator is limited to less than 5 min to avoid oxidation and taste-and-odour carryover. Wall thickness is 3.0 mm to 5.0 mm. The olefin polymer is listed under FDA 21 CFR 177.1520, and final-component certification is tested under NSF/ANSI 61 where cold water service is required. For European drinking-water components, overall migration is evaluated under EU 10/2011. Continuous water temperature should remain below 40 °C, and hydrostatic pressure should not exceed 0.5 bar. The grade is not a PE100 pipe extrusion resin and is not specified for pressure piping. Terminal products are brine tanks, media filter housings, and non-pressurised filter sumps for residential and light industrial water treatment equipment.
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Dow HDPE DMDB-7950 NT 7 is a natural-color high-density polyethylene homopolymer supplied in pellet form and formulated for high-molecular-weight blown film extrusion. The resin’s product code designates the HDPE series, while NT 7 denotes the natural pellet and additive configuration. The polymer is based on a bimodal molecular weight distribution that separates shear-thinning response during screw transport from extensional strength after the die annulus. Representative published nominal values include a melt flow rate of 0.08 g/10 min at 190 °C/2.16 kg under ISO 1133-1:2022, a high-load melt flow rate of 9.0 g/10 min at 190 °C/21.6 kg, and a density of 0.955 g/cm³ at 23 °C under ISO 1183-1:2019. The resulting I21/I2 melt flow ratio is approximately 112.5. These values are representative and lot-specific certificates of analysis control production acceptance.
| Property | Test method | Representative nominal value |
|---|---|---|
| Density at 23 °C | ISO 1183-1:2019 / ASTM D792 | 0.955 g/cm³ |
| Melt flow rate at 190 °C, 2.16 kg | ISO 1133-1:2022 / ASTM D1238 | 0.08 g/10 min |
| Melt flow rate at 190 °C, 21.6 kg | ISO 1133-1:2022 / ASTM D1238 | 9.0 g/10 min |
| Melt flow ratio I21/I2 | Calculated | 112.5 |
| Vicat softening temperature, A50 | ISO 306 / ASTM D1525 | 124 °C |
The material is primarily specified in monolayer and coextruded high-stalk HMW-HDPE film structures for grocery sacks, T-shirt sacks, can liners, merchandise bags, and industrial liners. In these applications, the combination of high melt strength and controlled orientation permits film thickness reductions while retaining bubble symmetry during commercial take-off. The resin is not a general-purpose low-viscosity HDPE; its low 2.16 kg melt flow rate restricts use in injection molding or extrusion blow molding where lower melt viscosity is required for fill pressure and parison sag control.
The low-molecular-weight fraction lowers shear viscosity during barrel transport, reducing extruder back pressure and enabling stable screw feeding on high-molecular-weight film lines. The high-molecular-weight fraction raises the zero-shear viscosity and produces a I21/I2 melt flow ratio near 112.5, which correlates with increased melt strength after die exit. On production-scale grooved-feed single-screw extruders with L/D ratios from 24:1 to 30:1, bubble chatter and stalk sag are observed less frequently than with unimodal HMW-HDPE grades when the die gap is maintained between 1.2 mm and 2.0 mm. However, the same rheological balance narrows the process window at melt temperatures below 190 °C. In that range, increased extensional viscosity can produce unstable stalk curvature, nonuniform frost line height, and fluctuation in transverse-direction film gauge. Published data for this specific configuration is limited; therefore, line-specific verification with a fixed die gap and blow-up ratio is required before dimensional tolerances are transferred from a reference grade.
In high-stalk monolayer bubble configuration, the resin supports a stable neck above the die, but the frost line height must be raised proportionally with throughput. At blow-up ratios between 3:1 and 5:1, film with a final thickness from 12 µm to 50 µm can be produced on conventional HMW-HDPE film lines. The die gap is typically held at 1.4 mm to 1.8 mm. Narrower gaps elevate die shear stress and may trigger melt fracture at the die lip, while wider gaps reduce machine-direction orientation and may lower machine-direction tensile yield measured under ISO 527-3. Barrel temperature profiles commonly range from 170 °C in the feed section to 220 °C at the die adapter, with melt temperature held between 190 °C and 230 °C. Operation above 240 °C accelerates gel formation and should be avoided. When surface moisture from condensation is present after storage at relative humidity above 70%, a 60 °C dehumidified-air purge for 1 h is typical for HMW-HDPE to restore granule surface condition. Regrind addition is common in bag applications, but industrial practice for HMW-HDPE film suggests that regrind fractions above 20 wt% may increase gel count and reduce dart impact; published data for this specific grade is limited.
Grocery sack and can liner structures are commonly specified at 12 µm to 25 µm final thickness. Dart impact resistance under ASTM D1709A is frequently used as a package-level control because it responds to gauge, orientation, and stress concentration. The density of 0.955 g/cm³ provides higher bending stiffness than HDPE film grades in the 0.940 g/cm³ to 0.948 g/cm³ density range, but the stiffness increase can reduce puncture energy absorption if the film is not adequately oriented. A blow-up ratio near 4:1 is often used to balance machine-direction and transverse-direction Elmendorf tear strength measured under ASTM D1922. When down-gauging from 25 µm to 12 µm, the reduction in dart impact follows a nonlinear thickness dependence. Published data for this specific configuration is limited; minimum allowable thickness must be established on the intended packaging line using ASTM D1709A dart impact and ISO 527-3 tensile protocols rather than by density alone. Compared with a 0.948 g/cm³ HMW-HDPE film resin, this grade can yield higher modulus at equal gauge, but it may require a wider die gap or adjusted frost line height to prevent transverse-direction tear loss in high-stalk operation.
For food-contact packaging, HDPE homopolymers of this type are generally evaluated under 21 CFR 177.1520(c) as olefin polymers and under EU Regulation (EU) No 10/2011 for plastic materials intended to contact food. These citations do not automatically certify the finished package; migration testing under EU Regulation (EU) No 10/2011 or FDA end-use conditions must be completed on the final structure, including any coextruded layers, printing inks, or adhesives. For non-food industrial sacks and can liners, compliance with REACH and RoHS Directive 2011/65/EU is documented through the manufacturer’s Safety Data Sheet and product compliance statement. Lot-specific verification is required for export to markets with additional food-contact or hazardous-substance restrictions. The resin is not supplied for medical implant use, and no claim under ISO 10993 is available absent written manufacturer confirmation.
Substitution of this resin into extrusion blow molding, sheet extrusion, or injection molding is not an equivalent replacement. Because the 2.16 kg melt flow rate is 0.08 g/10 min, the viscosity at typical injection molding shear rates is substantially higher than that of injection-molding HDPE grades with melt flow rates above 10 g/10 min. The high molecular weight and high melt strength are appropriate for blown film, but they generate excessive injection pressures and long cycle times in injection molds. Conversely, a low-viscosity film grade or an extrusion blow molding resin with a higher 2.16 kg melt index cannot reproduce the same bubble stability at thin gauge. The product also differs from conventional extrusion blow molding grades in the DMDA series, which are formulated for die swell and parison sag control rather than for high-stalk film bubble mechanics. For these reasons, direct grade substitution must be evaluated using the intended equipment type and the ISO 1133-1:2022 melt flow ratio, not density alone.