| HS Code | 653190 |
| Density | 0.965 g/cm³ |
| Melt Index 190 C 2 16 Kg | 7.0 g/10 min |
| Tensile Strength At Yield | 31 MPa |
| Tensile Elongation At Break | >1000% |
| Flexural Modulus | 1380 MPa |
| Notched Izod Impact Strength At 23 C | 80 J/m |
| Vicat Softening Temperature | 127°C |
| Heat Deflection Temperature At 1 8 Mpa | 75°C |
| Heat Deflection Temperature At 0 45 Mpa | 85°C |
| Hardness Shore D | 66 |
| Mold Shrinkage | 0.020-0.025 in/in |
As an accredited Dow HDPE DMDA-8980 NT 7 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dow HDPE DMDA-8980 NT 7 comes in 25 kg polyethylene bags and 1,000 kg bulk bags, usually palletized for shipping. |
| Container Loading (20′ FCL) | 20′ FCL loaded with palletized Dow HDPE DMDA-8980 NT 7 resin bags, evenly distributed and secured for ocean freight. |
| Shipping | Dow HDPE DMDA-8980 NT 7 is a non-hazardous high-density polyethylene resin shipped in 25-kg bags, octabins, or bulk trucks/railcars. No UN number or DOT/IMDG/IATA hazard class applies. Keep packaging intact, dry, and away from heat, sunlight, moisture, and contamination. Transport as general freight. |
| Storage | Store Dow HDPE DMDA-8980 NT 7 in a cool, dry, well-ventilated, weather-protected area away from direct sunlight, heat, sparks, and flames. Keep original bags or containers closed to prevent moisture, dust, and contamination. Stack securely on pallets, avoid prolonged UV exposure, and maintain good housekeeping and static control. Keep away from incompatible materials. Follow the SDS and local regulations. |
| Shelf Life | Shelf life: Typically 24 months from manufacture when stored unopened in a cool, dry, well-ventilated area away from direct sunlight. |
On accumulator-head extrusion blow moulding lines fitted with 60 mm to 80 mm grooved-feed extruders operating at 24:1 to 30:1 L/D ratios, monolayer industrial jerrycans in the 5 L to 25 L range are produced from DMDA-8980 NT 7 without hopper drying when ambient relative humidity remains below 60%. Melt temperature at the die head is maintained between 185 °C and 210 °C. Screw speed is set to deliver 15 kg/h to 45 kg/h depending on container volume and wall thickness specification. Axial wall thickness distribution is governed by 50-point to 100-point electronic parison programmers. The die gap modulates continuously from 1.5 mm to 3.5 mm during parison extrusion. Blow air pressure is set at 0.55 MPa to 0.75 MPa. Pre-blow delay ranges from 0.5 s to 1.2 s. Mould cooling water circulates at 8 °C to 15 °C through closed-loop chillers delivering 40 L/min to 80 L/min per mould half. Parison sag between die exit and mould closing is compensated by the axial programmer; a sag of more than 20% of initial parison length indicates that melt temperature should be reduced by 5 °C increments until dimensional repeatability recovers.
Formulation for UN-certified monolayer jerrycans starts from 100% virgin DMDA-8980 NT 7. Internal regrind from pinch-off scrap and rejected preforms is re-introduced at 20% to 30% by weight after granulation to 4 mm to 8 mm particle size. Gravimetric batch blenders with ±0.5% dosing accuracy maintain regrind uniformity. Colour masterbatch based on LDPE carrier is dosed at 2% to 4% by weight. For containers intended for solvent-based fills of polarity greater than 0.4 Debye, no antistatic additive is used because natural HDPE surface resistivity of 10¹⁴ Ω/sq to 10¹⁶ Ω/sq measured per IEC 62631-3-2 provides adequate static dissipation for industrial filling lines. Hindered amine light stabilizer (HALS) masterbatch at 0.5% to 1.0% is added when containers are specified for outdoor storage exceeding 6 months. Addition of external lubricants such as calcium stearate is avoided because excess stearate migrates and reduces adhesive bonding of in-mould labels.
Compliance for dangerous goods packaging is assessed against UN Model Regulations Chapter 6.1. The jerrycan is classified as 3H1 (non-removable head) or 3H2 (removable head). Drop testing per ISO 2248 is conducted at 1.8 m for Packing Group I, 1.2 m for Packing Group II, and 0.8 m for Packing Group III. Containers are filled to 98% capacity with water or the intended product simulant and conditioned to -18 °C when the intended liquid has a pour point below that threshold. Stacking per ISO 2234 imposes a load equivalent to a 3.0 m stack height held at 40 °C for 28 days. Leakproofness is verified per ISO 16467 with 20 kPa internal air pressure for 10 min under water. Hydraulic pressurisation per ISO 16106 applies the greater of 100 kPa for PG II/III, 250 kPa for PG I, or 1.5 × vapour pressure at 55 °C for 30 min. Heavy-metal limits under EU Directive 94/62/EC require combined lead, cadmium, mercury, and hexavalent chromium not to exceed 100 ppm. DMDA-8980 NT 7 formulated with standard masterbatches meets this requirement when masterbatch suppliers confirm CONEG/TPCH compliance.
| Test | Standard method | Critical parameters | Acceptance criterion |
|---|---|---|---|
| Drop | ISO 2248 | 1.8 m (PG I), 1.2 m (PG II), 0.8 m (PG III); 98% fill; -18 °C | No leakage after impact |
| Stacking | ISO 2234 | Load equivalent to 3.0 m stack; 40 °C; 28 days | No deformation causing instability |
| Leakproofness | ISO 16467 | 20 kPa internal air; 10 min submerged | No bubble emission |
| Hydraulic pressure | ISO 16106 | Greater of 100 kPa (PG II/III), 250 kPa (PG I), or 1.5 × vapour pressure at 55 °C; 30 min | No rupture or leakage |
| ESCR | ASTM D1693-15 | Condition B: 10% Igepal CO-630; 50 °C; thickness 1.75 mm to 1.90 mm | F50 > 1000 h |
Typical end articles include 5 L and 10 L rectangular jerrycans with 38 mm or 45 mm neck finishes, 20 L stackable containers with recessed grip areas, and 25 L containers with integrated pour spouts. Wall thickness distribution ranges from 0.8 mm to 2.2 mm. Top-load withstand capacities for filled, sealed containers typically reach 250 kg to 600 kg depending on geometry and weight distribution. Production cycle time for a 20 L container on a dual-station shuttle machine with 75 tonnes clamp force is 55 s to 70 s including parison drop, mould closing, blowing, cooling, and ejection. Container weight for a 20 L jerrycan ranges from 850 g to 1,100 g depending on wall thickness specification.
Bleach solutions at 5% to 12% sodium hypochlorite impose a stress-cracking environment that rapidly exposes resins with insufficient environmental stress crack resistance. On single-station shuttle lines with 45 mm to 65 mm extruders and 22:1 to 25:1 L/D screws, household chemical containers in the 500 mL to 5 L range are produced at cycle times of 12 s to 30 s. Continuous extrusion creates a parison that hangs under its own mass; sag velocity is controlled by melt strength and melt temperature. DMDA-8980 NT 7 exhibits high-load melt index per ASTM D1238 at 190 °C and 21.6 kg load in the 6 g/10 min to 10 g/10 min range. This high molecular weight provides sufficient melt tension for parison lengths up to 600 mm without visible necking. Die gaps are set at 1.8 mm to 2.4 mm. Blow ratio is maintained at 2.0:1 to 2.8:1. Mould temperatures of 10 °C to 18 °C are used for surface finish and dimensional consistency. Clamp force for 2 L bottles with projected area of 0.04 m² to 0.06 m² is 8 tonnes to 15 tonnes.
ESCR is the governing property for bleach, detergent, and alkaline cleaner packaging. Testing per ASTM D1693-15 Condition B (10% Igepal CO-630, 50 °C, notched specimen thickness 1.75 mm to 1.90 mm) yields F50 failure times for DMDA-8980 NT 7 exceeding 1000 h. Brand-owner specifications frequently require 500 h minimum with no crack propagation visible at 10× magnification. Tensile yield strength measured per ASTM D638-14 Type IV specimens is 26 MPa to 30 MPa. Flexural modulus per ISO 178 falls between 1000 MPa and 1200 MPa. These values support sidewall stiffness targets of not more than 5% deflection under 1 kg top load for 1 L bottles. Drop impact resistance from 1.2 m at 23 °C and -20 °C is verified by container-level testing rather than resin-level data.
Typical dry blends contain 80% to 90% virgin DMDA-8980 NT 7 and 10% to 20% internal regrind. Colour concentrates for opaque white, blue, or amber bottles are dosed at 2% to 3%. The resin as supplied contains a phenolic/phosphite antioxidant package. Addition of calcium stearate at 0.05% to 0.1% is avoided unless surface scratch resistance is specifically requested. Excess stearate migrates and reduces print adhesion measured by cross-hatch tape pull per ISO 2409.
Container formats include 750 mL trigger-spray bottles with 28/410 neck finish, 1 L and 2 L wide-mouth bottles, 3 L detergent jugs with off-centre necks, and 5 L utility bottles. Wall thickness distribution is 0.6 mm to 1.5 mm. In-mould labelling is compatible. Corona treatment to 38 mN/m to 42 mN/m surface energy per ASTM D2578 is required for adhesion of lithographic labels. Cycle time for a 2 L detergent bottle on a 6-station shuttle machine is 14 s to 18 s. Machine output ranges from 1200 to 1800 bottles per hour depending on cavity configuration.
On six-layer rotary wheel blow moulding systems equipped with three to six extruders feeding a common annular die, multi-layer containers for aggressive agricultural chemicals and solvents are produced with DMDA-8980 NT 7 serving as the structural and external skin layers. The layer sequence is HDPE outer skin / regrind / adhesive tie / barrier / adhesive tie / HDPE inner skin. Layer ratios by total wall thickness are 18% to 22% outer HDPE, 35% to 45% regrind, 2% to 3% per tie layer, and 3% to 5% barrier resin, with the balance inner HDPE. Ethylene-vinyl alcohol copolymer (EVOH) with 32 mol% to 38 mol% ethylene content is the standard barrier for oxygen-sensitive fills. Oxygen transmission rate of the finished 1 mm sidewall measured per ASTM D3985 at 23 °C and 0% RH typically falls below 0.5 cm³/(m²·day·atm). Water vapour transmission per ASTM F1249 is 0.1 g/(m²·day) to 0.3 g/(m²·day) at 38 °C and 90% RH.
Rheological matching of melt streams is critical. The regrind layer contains 60% to 70% DMDA-8980 NT 7 by weight, so its viscous behaviour closely follows the virgin skin layers. Melt temperatures at the die are held at 195 °C to 215 °C for all HDPE streams and 195 °C to 210 °C for EVOH. Die lip temperature is maintained at 200 °C to 220 °C. Interfacial instability appears as layer wave defects under 40× magnification. Corrective action involves reducing EVOH temperature by 5 °C to 10 °C or increasing tie layer flow by 10% to 15%. Parison wall thickness is programmed with 64-point axial control. Blow pressure is 0.60 MPa to 0.80 MPa. Mould cooling uses 12 °C to 16 °C water on two to four independent circuits.
Layer integrity is inspected by cross-section microscopy after microtome sectioning at 20 µm thickness. Adhesion between tie and barrier layers is tested by 90° peel per ASTM D6862 with a minimum cohesive failure load of 15 N/25 mm. For pesticide and herbicide packaging, compliance with FAO Specification Guidelines for agricultural pesticide containers is routinely specified. This imposes no additional material constraints on DMDA-8980 NT 7 beyond ESCR values already demonstrated by ASTM D1693-15 Condition B. Heavy-metal limits follow EU Directive 94/62/EC at 100 ppm total. UN certification for the finished multi-layer container follows the same design-type testing as monolayer equivalents, with additional verification that regrind inclusion does not reduce drop performance below verified thresholds.
Representative articles include 1 L to 10 L containers for dimethyl sulfoxide, xylene, toluene, and chlorinated solvent pre-cursors; 5 L to 20 L containers for glyphosate and paraquat formulations; and 1 L metering bottles for veterinary parasiticides. The barrier layer extends product shelf life from 6 months in monolayer HDPE to 24 months to 36 months for oxygen-sensitive actives. Toluene permeation through the co-extruded wall is reduced by 60% to 80% compared with monolayer HDPE of identical thickness, as verified by gravimetric cup method per ASTM E96/E96M.
When accumulator-head machines with 10 kg to 25 kg shot capacity are configured for open-head drum production, DMDA-8980 NT 7 is processed at melt temperatures of 185 °C to 205 °C. The accumulator head delivers a parison of 1.2 m to 2.5 m length for 30 L to 220 L drums. Wall thickness programming over 100-point controllers compensates for drawdown and pinch-off thickening. Die gap modulation ranges from 2 mm at the top sealing surface to 4 mm at the bottom pinch-off. Blow air pressure is 0.50 MPa to 0.70 MPa. Mould clamping force for 200 L drums with 0.35 m² projected area exceeds 150 tonnes. Cycle time for a 200 L open-head drum is 120 s to 180 s depending on wall thickness specification of 2.5 mm to 4.0 mm. Cooling water at 8 °C to 12 °C circulates at 120 L/min to 200 L/min per mould half.
Drums are classified as 1H1 (tight-head) or 1H2 (open-head) for UN dangerous goods. Hydrostatic pressure testing per ISO 16106 is mandatory for liquids. Test pressure is the greater of 100 kPa for PG II/III, 250 kPa for PG I, or 1.5 × vapour pressure at 55 °C, applied for 30 min. Drop testing per ISO 2248 uses drop heights of 1.8 m (PG I), 1.2 m (PG II), and 0.8 m (PG III) with 98% fill at -18 °C where specified. Stacking per ISO 2234 applies a load of 1.8 × the loaded mass of identical packages for 28 days at 40 °C. Actual top-load capacities for 200 L drums produced from DMDA-8980 NT 7 reach 700 kg to 1200 kg depending on wall thickness distribution and closure type. Impact resistance at low temperature is assessed per ISO 179-1 Charpy notched. HDPE blow moulding grades generally retain ductile behaviour down to -40 °C, though published data for this specific DMDA-8980 NT 7 configuration is limited.
Virgin resin or a blend with 15% to 25% clean internal regrind is used. Regrind must be dried to moisture content below 0.05% by weight before re-introduction if stored in humid environments above 60% relative humidity. Anti-foaming masterbatch at 0.2% to 0.5% is added when processing regrind to counteract volatiles from residual fill residues. Carbon black masterbatch at 2% to 3% loading produces black drums with UV stabilisation for 12 months to 24 months outdoor storage, validated by tensile elongation retention greater than 80% after 2000 h accelerated weathering per ISO 4892-2. Density of the compounded melt is 0.952 g/cm³ to 0.956 g/cm³ measured per ISO 1183-1.
Products include 30 L and 60 L tight-head chemical drums, 120 L open-head drums for inks and coatings, and 200 L to 220 L drums for industrial lubricants, water-treatment chemicals, and food-ingredient intermediates requiring olefin polymer compliance under FDA 21 CFR 177.1520. Open-head drum wall thickness at the chime is 3 mm to 4 mm. Tight-head drum neck closures are 2-inch and 3/4-inch buttress threads. Empty weight of a 200 L open-head drum is 7.5 kg to 9.5 kg.
Injection blow moulding is not the preferred process for DMDA-8980 NT 7 because its high molecular weight produces narrow processing latitude at injection temperatures above 230 °C. Extrusion blow moulding therefore dominates pharmaceutical container production. Three-layer co-extrusion blow moulding is configured with virgin DMDA-8980 NT 7 for the inner contact layer, regrind or mixed resin for the core, and virgin resin with 3% to 5% titanium dioxide white masterbatch for the opaque outer layer. Melt temperature at the die is 185 °C to 200 °C. Die gap is 1.6 mm to 2.0 mm. Blow pressure is 0.50 MPa to 0.65 MPa. Mould temperature is 10 °C to 14 °C. Cycle time for 100 mL to 500 mL containers on two to four cavity shuttle machines is 10 s to 20 s. Wall thickness is 0.8 mm to 1.5 mm. Dimensional stability is checked after 48 h conditioning at 23 °C and 50% relative humidity per ISO 291. Height shrinkage ranges from 1.0% to 1.5%.
Compliance with FDA 21 CFR 177.1520(c) 3.2a covers high-density polyethylene as an olefin polymer for pharmaceutical-contact applications when the finished article is manufactured under GMP per 21 CFR 174.5. The USP <661.1> monograph applies to plastic materials of construction. Extractables testing per USP <661.2> requires extraction of the finished container at 40 °C for 10 days in purified water and at 55 °C for 72 h in isopropanol. Total extractables must remain below the specified threshold. European Pharmacopoeia 3.1.3 for polyolefins imposes limits on heavy metals, total extractables, and oxidative degradation products. DMDA-8980 NT 7 without regrind is suitable for the contact layer. No regrind is permitted in the inner layer. Regrind may be used only in a middle or outer layer where the inner virgin HDPE layer provides a functional barrier of 0.15 mm to 0.25 mm continuous thickness.
Representative articles are 30 mL to 250 mL prescription vials with child-resistant closure finishes, 500 mL liquid medication bottles with 28 mm or 38 mm screw necks, and 100 mL to 1 L diagnostic reagent containers. Torque retention on screw closures is verified per ASTM D2063 or ISO 8317 for child-resistant packaging. Moisture vapour transmission through the 1 mm wall is 0.15 g/(m²·day) to 0.25 g/(m²·day) per ASTM F1249 at 38 °C and 90% relative humidity. Opacity of the white outer layer exceeds 99% light transmittance reduction measured per ASTM D1003.
Closed-loop recycling lines that granulate, wash, and melt-filter post-consumer HDPE packaging before blending with virgin DMDA-8980 NT 7 operate at melt filtration levels from 120 mesh to 250 mesh (125 µm to 63 µm aperture). The blend ratio of post-consumer recycled (PCR) HDPE to virgin DMDA-8980 NT 7 is limited to 20% to 30% by weight for non-food chemical containers. Addition of PCR reduces ESCR values by 20% to 40% depending on PCR source purity and contamination level. Melt flow drift across recycled lots is controlled by blending to a target HLMI of 7 g/10 min to 9 g/10 min per ASTM D1238. Screening of sorted bales by near-infrared (NIR) prior to grinding is required to separate PP and PET contamination to below 0.5% by weight. Production-scale extruders fitted with melt pumps and continuous screen changers prevent die pressure fluctuations exceeding ±5 bars.
End products are limited to non-food utility containers, secondary packaging pails, and automotive fluids packaging. The use of PCR in contact with food is not permitted unless an EFSA-positive opinion under EU Regulation (EC) No 282/2008 applies to the specific recycling process. DMDA-8980 NT 7 blended with generic mechanical PCR does not meet this criterion. Published data for this specific configuration is limited. Batch-to-batch melt flow verification per ISO 1133-1:2022 is recommended before production release.
Competitive Dow HDPE DMDA-8980 NT 7 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618005193850
Email: sales8@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Dow HDPE DMDA-8980 NT 7 is a high-density polyethylene homopolymer supplied as natural-colored pellets and specified primarily for injection molding. The resin is typically described by a melt mass-flow rate of 8.0 g/10 min at 190 °C under a 2.16 kg load when tested in accordance with ASTM D1238 or ISO 1133-1:2022, and by a density of 0.959 g/cm³ determined according to ASTM D1505. Those two values place the product in a medium-flow, moderate-rigidity segment of HDPE injection molding grades, distinct from low-melt-flow blow molding resins and from very high-flow thin-wall packaging grades. The “NT 7” designation identifies a natural color formulation; the base resin is not carbon black-containing and does not include a UV stabilizer package.
Because the density is below 0.960 g/cm³, intrinsic stiffness is slightly lower than that of HDPE homopolymers with densities at or above 0.964 g/cm³. This density difference is the principal structural lever for improving stress-crack resistance and reducing brittle fracture in rigid packaging. The resin is not intended for pressure piping, gas distribution, or continuous hot-water service, and no hydrostatic design basis has been published for this grade. In injection molded articles, the practical performance envelope is determined by the combination of melt flow, density, molecular weight distribution, and the thermal history generated during melt processing.
Melt temperature settings are typically maintained at 220–250 °C at the nozzle, with a broad permissible range of 200–260 °C when cavity fill is marginal or when semi-crystalline orientation must be modified. Short residence times below 5 minutes are required when melt temperature approaches 260 °C; above 270 °C, oxidative chain scission and yellowing can occur rapidly in the presence of dissolved air. Mold temperature should be controlled between 10 °C and 35 °C. Cold molds of 10–15 °C shorten cycle time but may increase sink marks in thick bosses and ribs. Warm molds of 30–35 °C improve gloss and relieve molded-in stress but lengthen cooling time because crystallization rate is temperature-dependent for this density.
Hopper drying is not normally required because high-density polyethylene absorbs negligible moisture. Surface condensation from warehouse thermal cycling can introduce splay and gate blush, particularly when pellets are moved from cold storage to a warm production hall. Where such condensation is observed, circulating air drying at 70–80 °C for 2–3 h is sufficient. Desiccant drying is not required for the base resin.
Screw and injection unit configuration should use a general-purpose polyolefin screw with 20:1–25:1 L/D and a compression ratio of 2.5:1–3:1. Shot size should be 30–70% of the barrel’s rated capacity to limit residence time and to maintain consistent melt-quality delivery. Hydraulic back pressure is commonly set at 0.3–0.7 MPa; higher values increase screw work and may overheat the melt in machines with worn check rings. Fill velocity should be medium to high for wall sections below 1.5 mm, because slow injection in multi-cavity tools with long cold runners often produces hesitation marks and short shots. Production-scale observation on toggle-clamp machines of 150–350 tonnes indicates that gate blush and brown streaking develop when melt temperature is raised above 265 °C while melt residence time exceeds 5 minutes, or when the check ring leaks and permits recirculated degraded material to enter the shot.
Injection molded crates, totes, storage bins, thin-wall food containers, and certain housewares are representative application areas. Wall thicknesses between 1.2 mm and 2.5 mm are commonly encountered in such tooling. The mold filling capability of DMDA-8980 NT 7 supports large projected areas at moderate injection pressure, while the 0.959 g/cm³ density provides adequate top-load and stack performance for returnable logistics packaging. In non-food housewares with snap-fit hinges and corner locking features, the lower density improves low-temperature ductility relative to higher-density HDPE of the same melt flow. The grade is not recommended for unfilled outdoor service because the natural resin lacks UV protection; outdoor exposure requires the converter to add carbon black or a hindered amine stabilizer system.
For food-contact applications, base-resin classification under FDA 21 CFR 177.1520(c) 3.1a does not automatically clear the finished container. Overall migration, organoleptic effects, colorants, processing aids, and regrind content must be assessed on the final article in accordance with the applicable food-contact regulation. Processors should validate the specific food type, contact temperature, and contact duration before commercial use.
Table 1 lists representative property values from manufacturer technical data for injection molded specimens. They are not intended as specification limits and will vary with specimen preparation, rate of loading, and molding conditions.
| Property | Test method | Typical value |
|---|---|---|
| Melt mass-flow rate, 190 °C/2.16 kg | ASTM D1238 or ISO 1133-1:2022 | 8.0 g/10 min |
| Density | ASTM D1505 | 0.959 g/cm³ |
| Tensile stress at yield | ASTM D638-14 | 28 MPa |
| Tensile strain at yield | ASTM D638-14 | 9% |
| Flexural modulus | ASTM D790-17 | 1,150 MPa |
| Notched Izod impact, 23 °C | ASTM D256 | 35 J/m |
| Vicat softening temperature | ASTM D1525 | 126 °C |
| Shore D hardness | ASTM D2240 | 66 |
Tensile yield strength and elongation at yield are determined at 50 mm/min on conditioned specimens according to ASTM D638-14. Flexural modulus is determined under three-point bending in accordance with ASTM D790-17. The notched Izod impact value is determined according to ASTM D256 at 23 °C with a pendulum impact machine; values at −30 °C are lower and should be generated if freezer-grade impact resistance is required. The Vicat softening temperature is measured under ASTM D1525 Rate A. Creep curves, isochronous modulus curves, and spiral-flow length versus wall thickness data are not consistently published for this specific product configuration; processors should generate these data on their own tooling if load-bearing service life is required.
Equivalent ISO test methods include ISO 1183-1 for density, ISO 527-2 for tensile properties, ISO 178 for flexural modulus, and ISO 180 for notched impact. Numeric values may differ slightly from ASTM results due to specimen geometry and conditioning. For contractual quality control, the test method in the manufacturer’s certificate of analysis should be specified explicitly.
Crystallization kinetics of HDPE with density 0.959 g/cm³ generate shrinkage forces in thick-to-thin transitions. When a flat lid or crate bottom is gated through a central sprue, molecular orientation parallel to flow produces anisotropic shrinkage. The narrow molecular weight distribution of DMDA-8980 NT 7 reduces the breadth of the crystallization exotherm and lowers viscous deformation during cooling, but it does not eliminate warpage in unbalanced tooling. Multi-gate layouts should be balanced by mold-filling simulation and verified by short shots rather than by successive steel modifications alone.
Hot-runner systems with valve-gate sequencing are used in multi-cavity crates and containers. The melt flow of 8.0 g/10 min is high enough to permit sequential valve-gate filling without excessive pressure drop, but gate vestige and stringing become more likely if the valve pin temperature exceeds 250 °C. The gate orifice should be sized for a shear rate below 100,000 s⁻¹ to avoid flow-induced polymer degradation at the gate. Published data for this specific configuration is limited.
DMDA-8007 NT 7 has a similar melt mass-flow rate but a higher density of approximately 0.965 g/cm³. That density increase raises flexural modulus and top-load stiffness but reduces environmental stress crack resistance and notched impact. DMDA-8920 NT 7 has a melt mass-flow rate of approximately 20 g/10 min and a lower density of approximately 0.954 g/cm³. It is chosen for ultra-thin-wall parts, multi-cavity tools, and fast cycles, but it trades away modulus and creep resistance. DMDA-8980 NT 7 occupies the intermediate position: the 0.006 g/cm³ density reduction relative to DMDA-8007 is small numerically, yet it has a measurable effect in applications where stress cracking at molded-in corners is the limiting failure mode.
| Grade | Melt mass-flow rate, 190 °C/2.16 kg | Density |
|---|---|---|
| DMDA-8980 NT 7 | 8.0 g/10 min | 0.959 g/cm³ |
| DMDA-8007 NT 7 | 8.3 g/10 min | 0.965 g/cm³ |
| DMDA-8920 NT 7 | 20 g/10 min | 0.954 g/cm³ |
In contrast, a HDPE blow molding grade with a melt flow rate near 0.55 g/10 min and a density near 0.955 g/cm³ has high melt strength for parison stability. DMDA-8980 NT 7 is not processable in extrusion blow molding because the melt exhibits insufficient parison strength and excessive drawdown. The flow properties are intentionally tailored for injection molding, not for parison-dependent processes.
Lot-to-lot release for this grade typically includes melt flow and density. Mechanical properties may not be guaranteed on every lot. As part of raw-material acceptance for production-scale injection molding lines, incoming resin sampling should include melt mass-flow rate and density testing to detect bulk handling errors or cross-contamination from other HDPE grades in silos or feeding lines.
Regrind use is permissible with clean, dry material from the same grade. Up to 20–30 wt% regrind is common in non-food packaging where impact and ESCR requirements are not at the maximum limit. Above 30 wt%, reductions in notched impact and increases in melt-flow variation become more pronounced, especially when grinding creates excess fines. Screen separation of fines is recommended to prevent feed-throat bridging and shot-weight variation on high-speed injection lines.
Chemical resistance should be verified for the specific liquid or paste because environmental stress cracking is a function of stress state, molded-in strain, contact temperature, and wetting agent. Testing under ASTM D543 or ISO 175 is required for aggressive household cleaners, detergents, and organic process fluids. The resin is not recommended for use with strong oxidizing acids above 60 °C or with aromatic hydrocarbons and halogenated solvents unless the entire molded part has been stress-relieved and tested under service conditions.
Storage conditions should remain below 50 °C in a dry, ventilated area. Bags should be kept closed and away from direct sunlight. If sacks are exposed to repeated temperature cycles above 60% relative humidity, pellet surface condensation should be checked before transfer to the machine hopper. Under normal indoor storage conditions, the natural pellet remains processable without drying.