Dow Hdpe Dmdc 1210 Nt 7

Dow HDPE DMDC-1210 NT 7

    • Product Name: Dow HDPE DMDC-1210 NT 7
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 808783
    Density 0.954 g/cm³
    Melt Flow Rate 0.50 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 27.6 MPa
    Tensile Strength At Break 24.1 MPa
    Elongation At Break 600%
    Flexural Modulus 1.10 GPa
    Tensile Modulus 1.10 GPa
    Notched Izod Impact Strength 0.530 J/cm
    Vicat Softening Point 124°C
    Deflection Temperature At 0 45 Mpa 71°C
    Brittleness Temperature < -70°C
    Shore D Hardness 64
    Environmental Stress Crack Resistance 1000 h
    Melt Temperature 190-230°C
    Mold Temperature 20-60°C
    Mold Shrinkage 0.015-0.025 cm/cm

    As an accredited Dow HDPE DMDC-1210 NT 7 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Dow HDPE DMDC-1210 NT 7 is supplied in 25 kg polyethylene bags, typically palletized and shrink-wrapped for industrial transport and storage.
    Container Loading (20′ FCL) 20′ FCL loads Dow HDPE DMDC-1210 NT 7 at about 25 MT in 25 kg bags, or 20 MT palletized.
    Shipping Dow HDPE DMDC-1210 NT 7 ships as a non-hazardous, high-density polyethylene resin in pellet form. It is not classified as dangerous goods for DOT, IMDG, IATA, or ADR transport. No UN number is required. Package in sealed bags, totes, or bulk containers; keep dry, avoid contamination, and protect from UV exposure.
    Storage Store Dow HDPE DMDC-1210 NT 7 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags/containers closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and excessive stacking. Maintain clean, stable ambient conditions and follow the manufacturer’s SDS and local regulations. Use first-in, first-out stock rotation.
    Shelf Life Shelf life is approximately two years from date of manufacture when stored unopened in original packaging under cool, dry conditions.
    Application of Dow HDPE DMDC-1210 NT 7

    In thin-wall injection moulding of dairy packaging and deli containers, DMDC-1210 NT 7 is processed with the melt temperature at the nozzle controlled between 220 °C and 235 °C. The grade’s nominal density of 0.956 g/cm³ (ASTM D1505) and melt flow rate of 12 g/10 min at 190 °C/2.16 kg (ISO 1133-1:2022) enable filling of sidewalls from 0.45 mm to 0.80 mm. A hot-runner manifold is maintained at 235 °C to 245 °C. Valve gates or thermal gates from 0.6 mm to 1.2 mm provide gate freeze times below 1.0 s. Back pressure is set between 5 bar and 10 bar hydraulic. Screw speed is 80–120 min⁻¹. The screw geometry is a general-purpose polyolefin design with 20:1 to 24:1 L/D ratio and compression ratio 2.5:1 to 3:1. If condensation is present, the granulate is dried for 2 h at 80 °C in a desiccant dryer. Packing pressure is initially 60 % to 80 % of peak injection pressure and is reduced after the part-weight plateau is reached. The shot size occupies 40 % to 70 % of barrel capacity. For coloured food-contact containers, a white masterbatch addition between 2 wt% and 4 wt% is typical. The masterbatch carrier is an HDPE or LDPE with food-contact status, and the colorant approval is referenced to 21 CFR 178.3297. Final sidewall and rim tolerances are checked at 24 h after moulding at 23 °C and 50 % RH.

    Regulatory frameworkRelevant provisionPractical verification
    U.S. FDA21 CFR 177.1520(c) for olefin polymersSupplier food-contact declaration; final article extraction test if coloured
    European UnionEU 10/2011 as amended by (EU) 2020/1245Overall migration < 10 mg/dm² under specified simulant and time/temperature conditions
    REACH(EC) No 1907/2006, Annex XVIISVHC content < 0.1 wt% per article; documentation in SCIP database
    Colorants21 CFR 178.3297Masterbatch TiO₂ and pigment approval letter

    Compliance of the final article is not automatically inherited from the resin. The processor must obtain a supplier food-contact declaration, and migration testing is performed on the finished package with the intended food simulant under time and temperature conditions specified by EU 10/2011. For U.S. distribution, 21 CFR 177.1520(c) covers olefin polymers, but the presence of colour concentrates, lubricants, or mould release agents must be assessed separately. The natural grade should not be mixed with regrind from non-food packaging without documented source control.

    What Limits Gate Freeze Time in 28 mm Closure Moulding?

    Closure manufacture with DMDC-1210 NT 7 uses the high-flow character of the resin when the tamper-evident band and sealing plug are filled through a single sub-gate or edge gate. In a 28 mm PCO 1810 closure, the outer shell wall is 0.9 mm to 1.2 mm, the tamper-evident band is 0.5 mm to 0.8 mm, and the sealing plug is 1.2 mm to 1.8 mm. Injection speed at the screw is set between 80 mm/s and 140 mm/s. The gate diameter is 0.8 mm to 1.5 mm. Packing pressure is 30 MPa to 50 MPa. The melt temperature is 235 °C to 250 °C. Mould temperature is 10 °C to 20 °C. Gate freeze time is measured by cavity pressure decay and part-weight plateau, not by hydraulic timers. A gate freeze time below 0.8 s may cause underpacking of the sealing plug and subsequent leakage. A freeze time above 2.0 s increases cycle time without benefit. The tamper-evident band uses eight to twelve break bridges with a thickness of 0.20 mm to 0.35 mm and a width of 2 mm to 4 mm. After moulding, closures are conditioned for 24 h at 23 °C before diameter and thread geometry are checked. Roundness variation is maintained below 0.15 mm by uniform cooling. Torque removal values are tested between 1.0 N·m and 2.5 N·m depending on the neck finish and liner type. The high-flow HDPE grade is not suitable for carbonated soft drink closures where internal pressure exceeds 4 bar, because the stress crack resistance of a high-flow injection moulding grade may be lower than that of a bimodal high-molecular-weight HDPE. The processor should avoid amine-based antistatic additives that can alter cap friction and torque retention.

    Open-top pail production with DMDC-1210 NT 7 uses sidewalls between 1.5 mm and 2.0 mm and a bottom thickness of 1.8 mm to 3.0 mm. The melt temperature is set at 240 °C to 260 °C to improve weld line strength around the handle holes. The mould temperature is 15 °C to 25 °C. For a 20 L pail with a projected area of 0.15 m², a cavity pressure of 35 MPa to 50 MPa requires a machine clamp force between 1,500 kN and 2,200 kN. The calculated clamp force includes runner and sprue projected area. Peak injection pressure at the machine is commonly 90 MPa to 120 MPa; only a portion reaches the cavity because of pressure drop through the nozzle, sprue, and runner. A cold runner diameter of 5 mm to 8 mm and a sprue bushing taper of 2° to 3° are used. If a hot-runner manifold is installed, it is heated to 240 °C to 250 °C. The moulded-in handle requires a side action and core pull sequence. The flow fronts merge on the opposite side of the handle aperture and form a weld line. Weld line strength is improved by raising melt temperature and by moving the gate away from the handle zone. The remaining wall around the handle opening is at least 1.8 mm, and the corner radius is not less than 2 mm. Total height tolerance is held to ±0.5 mm. Post-mould shrinkage is measured after 48 h at 23 °C and 50 % RH per ISO 294-4. The machine cushion is maintained between 3 mm and 6 mm. DMDC-1210 NT 7 is not suitable for extrusion blow moulding; the high melt flow leads to parison length instability. If the pail is used for food ingredients or emulsions, the additive package must be checked for organoleptic effects and migration limits.

    Crate Rib Fill Ratio and Warpage After Ejection

    For moulded logistics crates and ventilated tote boxes, the load-bearing floor is designed with orthogonal ribs that intersect flow fronts from multiple gates. DMDC-1210 NT 7 fills rib sections of 0.8 mm to 1.6 mm thickness when the nominal wall is 2.0 mm to 3.0 mm. The rib-to-nominal-wall ratio is kept between 0.5 and 0.7 to prevent sink marks on the top surface. Aeration slots with a width of 3 mm to 5 mm reduce material consumption and cooling time but create weld lines. The gates are located so that flow fronts meet at an included angle of 30° to 60° to avoid weak notched welds. Melt temperature is 240 °C to 260 °C. Mould temperature is 15 °C to 25 °C. For a flow path up to 350 mm and wall thickness above 2.0 mm, the high flow of 12 g/10 min permits filling before freeze-off. Peak injection pressure is 80 MPa to 120 MPa. A cold runner length of 200 mm can produce 20 MPa to 30 MPa pressure drop; runner diameter is therefore not reduced below 5 mm. Floor gates of 1.2 mm to 2.0 mm diameter prevent short-shot defects at the rib tips. Post-ejection warpage is measured as the deviation of the four bottom corners from a flat granite table after 48 h at 23 °C. For a 600 mm × 400 mm crate, the maximum allowable corner deflection is generally 3 mm to 6 mm depending on the stacking requirement. Differential shrinkage between the floor and sidewalls is reduced by ensuring ejection temperature is below 80 °C and by cooling the gate area with sufficient flow. A dimensional audit uses a coordinate measuring machine referenced to the mould base datum, not to the moving ejector side.

    If Aesthetic Surfaces Are Moulded Without Texturing Agents

    Houseware articles such as storage boxes, trays, and bins require surface uniformity, colour permanence, and dimensional stability. DMDC-1210 NT 7 in natural form has high gloss when injected against a polished cavity. That gloss reveals sink marks, gate blush, and flow lines. If a textured cavity surface is not used, the processor must reduce gloss and hide surface defects by controlling melt temperature, mould temperature, and injection velocity. The melt temperature is set at 230 °C to 250 °C. The mould temperature is held between 15 °C and 25 °C. The initial injection stage is run at 80 mm/s to 120 mm/s to avoid jetting and gate blush. Colour masterbatch is added at 1 wt% to 3 wt% using a single-screw dosing unit. The screw should have a mixing zone or distributive mixing elements because the high-flow melt has limited back mixing. If the article is intended for children’s use, the applicable standard is EN 71-3:2019 for migration of certain elements. The resin alone does not ensure toy safety; the finished article must be tested. For food-contact houseware storage containers, the same FDA and EU migration limits apply. The natural grade lacks sufficient weatherability for long-term outdoor exposure. If the product is positioned for outdoor storage, a UV masterbatch containing HALS and carbon black at 2 wt% to 3 wt% is required, and dispersion must be verified by optical microscopy. The article is ejected at 70 °C to 80 °C and cooled uniformly on a flat surface. Dimensional changes are recorded after 72 h at 23 °C and 50 % RH for acceptance testing.

    Appliance Coupling Thread Retention Is Strain-Rate Dependent

    Appliance parts, including washing machine drain traps, dishwasher spray arm mounts, and refrigerator shelf brackets, require bolt thread retention and vibration resistance. DMDC-1210 NT 7 is used where complex geometry and short cycle times favour an injection moulding grade over sheet metal or polypropylene. The thread retention force in HDPE is strain-rate dependent; at 23 °C a test speed of 5 mm/min according to ISO 527-2 provides higher maximum stress than a test speed of 50 mm/min because the polymer is viscoelastic. A screw boss with a diameter of 6 mm and a thread engagement of 8 mm is typical for M4 self-tapping screws. The boss wall thickness is not less than 2 mm to prevent circumferential cracking. A minimum edge distance of 3 mm from the boss to the nearest wall is maintained. The root radius at the boss base is not less than 0.8 mm. Mould temperature is 20 °C to 30 °C, which improves crystallinity and dimensional stability but increases cycle time. Melt temperature is 240 °C to 260 °C. The material is not recommended for press-fit connections where interference exceeds 0.5 mm on a 20 mm diameter, because stress relaxation at 80 °C may reduce retention force. Snap-fit engagement is possible but strain should remain below 3 % to avoid stress whitening. The grade is not supplied as a flame-retardant system; under UL 94 testing it will not meet V-0 without high filler levels that degrade impact. If the appliance part requires detergent contact at 60 °C to 70 °C, published ESCR data for this specific DMDC-1210 NT 7 configuration is limited. A constant-strain test using 10 % Igepal CO-630 at 50 °C according to ASTM D1693 may be required to qualify the application. The processor should avoid adding non-food-grade mould release agents if the part is used in potable water contact.

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    Certification & Compliance
    More Introduction

    The resin identified as Dow HDPE DMDC-1210 NT 7 is a high-density polyethylene injection-molding grade supplied in natural pellet form. The grade is situated in the high-flow segment of HDPE, with a nominal melt flow index of 12 g/10 min at 190 °C/2.16 kg per ASTM D1238 and a nominal density of 0.961 g/cm³ per ASTM D792. These two values define the primary processing and property envelope: low melt viscosity for rapid filling of thin-wall cavities and high crystalline fraction for flexural stiffness. Typical application categories include thin-wall food-service containers, housewares, crates, trays, caps and closures, and general-purpose injection-molded components. The natural designation indicates that no full color package is incorporated, allowing press-side addition of color concentrate. Published technical literature for the material emphasizes injection-molding productivity and dimensional stability rather than long-term environmental stress-crack resistance.

    The following table lists nominal physical and mechanical data from supplier literature. The listed values are typical properties, not manufacturing specifications, and the cited ISO method counterparts may use different specimen geometry or conditioning; direct numerical equivalence should not be assumed.

    PropertyTest MethodNominal Value
    Melt flow index (190 °C/2.16 kg)ASTM D1238 / ISO 1133-1:202212 g/10 min
    DensityASTM D792 / ISO 1183-1:20190.961 g/cm³
    Tensile strength at yieldASTM D638 / ISO 527-232 MPa
    Tensile elongation at breakASTM D638 / ISO 527-212%
    Flexural modulusASTM D790 / ISO 1781,590 MPa
    Notched Izod impact at 23 °CASTM D256 / ISO 180/A22 J/m
    Shore D hardnessASTM D2240 / ISO 86868
    Vicat softening temperatureASTM D1525 / ISO 306129 °C
    Deflection temperature under load at 0.455 MPaASTM D648 / ISO 75-279 °C

    What Distinguishes DMDC-1210 NT 7 from High-Molecular-Weight HDPE Blow Molding Grades?

    The molecular architecture of DMDC-1210 NT 7 is characterized by a narrow molar mass distribution and low comonomer content. The high density of 0.961 g/cm³ indicates a crystalline fraction above that of typical high-ESCR HDPE with densities near 0.950 g/cm³. The higher crystalline fraction improves flexural modulus but decreases chain mobility and environmental stress-crack resistance. A melt flow index of 12 g/10 min corresponds to substantially lower zero-shear viscosity than HDPE blow molding or film grades with melt flow indices in the range of 0.2–1.0 g/10 min. The resin is therefore unsuitable for extrusion blow molding because the parison can sag under its own weight; high-molecular-weight blow molding grades retain parison stability but require higher head pressures and longer cooling times.

    Under ASTM D1693 Condition B, the grade's environmental stress-crack resistance is typically below 10 h, whereas high-molecular-weight blow molding HDPE with melt flow indices near 0.3 g/10 min commonly exceeds 600 h. This difference is not a defect; it is a consequence of molecular weight selection for injection-molding productivity. A blow molding HDPE with density 0.952 g/cm³ and MFR 0.3 g/10 min may exhibit flexural modulus near 1,200 MPa, compared with approximately 1,590 MPa for DMDC-1210 NT 7. The difference in modulus is driven primarily by crystallinity rather than molar mass.

    Rheological and Thermal Boundaries in Thin-Wall Injection Molding

    On injection molding lines using 20:1 to 24:1 L/D general-purpose screws with compression ratios of 3.0:1 to 3.5:1, the high melt flow index translates into shorter screw recovery and lower peak injection pressure relative to 5 g/10 min HDPE. Barrel temperatures from 200 °C to 230 °C are common, with nozzle settings at 210 °C to minimize stringing and drool. Mold temperatures between 20 °C and 40 °C are sufficient for dimensional stability in thin-wall parts; a mold-temperature increase to 60 °C improves knit-line strength and surface gloss but extends cooling time.

    Flow-front velocity should be controlled at 200–400 mm/s for wall sections below 1.5 mm. Published data for this specific configuration is limited; molders should establish the gate-freeze time using cavity-pressure transducers because packing time affects sink depth and shot mass. Holding pressure is typically 50–70% of peak injection pressure, with back pressure maintained below 1.5 MPa hydraulic to avoid excessive shear heating and molecular-weight degradation. The high-density grade exhibits mold shrinkage in the range of 0.015–0.030 mm/mm under ASTM D955, but the exact value varies with gate type, wall thickness, and molecular orientation. Differences between flow-direction and cross-flow shrinkage are a known source of warpage in flat lids and should be addressed through gate placement and uniform cooling rather than through excessive packing pressure alone.

    Drying is not generally required for HDPE because the polymer is non-hygroscopic. However, cold pellets exposed to humid air can accumulate surface condensation; if surface moisture is observed, drying at 80 °C for 2–4 h in a desiccant dryer is sufficient. The grade should not be processed in machines with deep-flight screws optimized for low-MFI HDPE, because over-shearing can generate melt temperatures above 240 °C and increase degradation risk.

    Comparative selection among HDPE injection and blow molding grades is governed by a trade-off between melt flow, rigidity, and stress-crack resistance. The following table presents published typical ranges for DMDC-1210 NT 7 and two reference HDPE categories; the reference values are not product specifications but reflect commercial resin families.

    Resin CategoryNominal MFR (g/10 min, 190 °C/2.16 kg)Nominal Density (g/cm³)Flexural Modulus (MPa)ESCR Condition B (h)
    DMDC-1210 NT 7 injection grade120.9611,590<10
    High-molecular-weight blow molding HDPE0.30.9521,200>600
    High-ESCR injection HDPE1.00.9501,100>100

    The difference relevant to part design is that DMDC-1210 NT 7 sacrifices ESCR and melt strength for increased melt flow and higher density. For dry impact applications, the higher modulus provides greater load-bearing capacity at equivalent wall thickness. For applications involving continuous stress and aggressive wetting agents, a high-molecular-weight or high-ESCR grade is required. The notched Izod impact value of 22 J/m is characteristic of high-density injection HDPE and is lower than that of many lower-crystallinity HDPE grades; designers should use instrumented multi-axial impact testing according to ASTM D3763 where crate or tray performance is dominated by puncture or drop loading.

    When Recyclate Dilution Changes Impact Behaviour in Crates and Pallets

    When post-industrial or post-consumer HDPE recyclate is blended with DMDC-1210 NT 7 at levels above 20 wt%, the melt flow index may shift upward or downward depending on the recycle feedstock. The notched impact strength can decrease more rapidly than predicted by linear mixing rules if the recyclate contains carbonyl-bearing degraded polymer, because chain scission lowers the molar mass of the blend. Injection molders running twin-screw extruders with 32:1 L/D compounding lines should monitor melt pressure before screen changers; pressure excursions above 20% of the virgin baseline indicate contaminant accumulation and require screen-pack maintenance.

    Regrind from sprues and runners is commonly used at 10–20 wt%. Physical properties are largely retained if the regrind is not thermally degraded and remains free of moisture. Multiple heat histories can increase yellowness; color-sensitive applications should limit closed-loop regrind to 15 wt% and use effective venting during melt preparation. At higher recyclate levels, environmental stress-crack resistance is further reduced, making chemical compatibility evaluations under ASTM D543 mandatory for detergents, alcohols, and aggressive food simulants. The grade should not be selected for sustained load-bearing pipe or fuel tank applications because of its low ESCR.

    Regulatory and compliance status for DMDC-1210 NT 7 must be verified against current supplier documentation. For food contact, the base polyethylene formulation is typically designed to comply with 21 CFR 177.1520 for olefin polymers and with Commission Regulation (EU) 10/2011 as amended, including the overall migration limit of 10 mg/dm² for plastic materials. Compliance is condition-specific; the converter is responsible for testing the finished article under EN 1186 or appropriate food-simulant protocols. The product is not inherently UV-stabilized; outdoor uses requiring extended weatherability should incorporate carbon black or a suitable stabilizer masterbatch. Under REACH Regulation EC 1907/2006, the resin is a polymer and is generally exempt from registration, though monomer and additive constituents must be registered where applicable. For electrical and electronic equipment, RoHS Directive 2011/65/EU applies to the final article rather than to the bulk resin supply. Storage should avoid direct flame and prolonged exposure to high ambient temperatures; if stored in a humid environment, surface condensation must be managed as described above.

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