Dow Hdpe Dmdh 6400 Nt 7

Dow HDPE DMDH-6400 NT 7

    • Product Name: Dow HDPE DMDH-6400 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 922344
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.961 g/cm³
    Melt Index 0.70 g/10 min
    Tensile Strength At Yield 29 MPa
    Tensile Strength At Break 22 MPa
    Elongation At Break 600%
    Flexural Modulus 1200 MPa
    Vicat Softening Point 127°C
    Heat Deflection Temperature 75°C at 0.45 MPa
    Environmental Stress Crack Resistance >1000 h
    Shore D Hardness 65
    Melting Point 134°C
    Thermal Conductivity 0.45 W/m·K
    Coefficient Of Linear Thermal Expansion 1.2E-4 /°C
    Water Absorption <0.01%
    Bulk Density 0.58 g/cm³

    As an accredited Dow HDPE DMDH-6400 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 DMDH-6400 NT 7 is supplied in 25 kg polyethylene bags, available in 1,375 kg pallet quantities.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Dow HDPE DMDH-6400 NT 7, 25 kg bags, palletized, shrink-wrapped, approximately 20 MT net per container.
    Shipping Dow HDPE DMDH-6400 NT 7 is a non-hazardous, solid high-density polyethylene resin. Ship in sealed 25 kg bags or bulk containers, protecting from moisture, heat, and contamination. Use standard freight; not regulated for transport, with no UN number, hazard class, or packing group required.
    Storage Store Dow HDPE DMDH-6400 NT 7 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep original bags or containers tightly closed, stacked securely on pallets, and protect from moisture, dust, and contamination. Follow manufacturer’s SDS, local regulations, and good housekeeping practices. Use appropriate PPE when handling.
    Shelf Life Recommended shelf life is 24 months when stored in original, unopened packaging under dry, cool conditions away from direct sunlight.
    Application of Dow HDPE DMDH-6400 NT 7

    When 3D Suction Blow Moulding Replaces Stamped Steel in Fuel Tank Architecture

    Dow HDPE DMDH-6400 NT 7 is specified for monolayer and multilayer automotive fuel tanks produced on long-stroke accumulator-head blow-moulding machines with 3D parison manipulation. The grade has a nominal density of 0.964 g/cm³ determined under ASTM D792 and a melt flow rate of 0.60 g/10 min at 190 °C/2.16 kg determined under ASTM D1238. In production-scale trials, melt temperatures are maintained between 180 °C and 210 °C; excursions above 220 °C for more than 10 min lower molecular weight and reduce environmental stress-cracking resistance enough to shift ASTM D1693 condition B results below automotive validation thresholds. The parison is extruded through a diverging die gap of 15–35 mm on an 80–120 mm grooved-feed extruder with L/D 24–30, then preblown at 0.05–0.20 MPa and final-blown at 0.6–0.9 MPa in aluminium moulds held at 10–20 °C.

    Formulation adjustments are determined by wall structure. In monolayer fuel tanks, carbon black masterbatch is added at 2.0–3.0 wt% for ultraviolet stabilization, processing aid at 0.05–0.15 wt%, and post-industrial regrind is capped at 20 wt% unless the moulder validates higher ratios against ASTM D638 tensile yield and ASTM D1693 condition B ESCR retention. In six-layer coextruded tanks, the EVOH barrier layer generally constitutes 1.5–3.0 wt% of total wall thickness, tie layers 1.0–2.0 wt%, outer high-density polyethylene 20–30 wt%, inner high-density polyethylene 20–30 wt%, and regrind 35–45 wt%; the regrind layer is positioned between the barrier and the outer or inner skin to preserve barrier continuity. Pre-drying at 70 °C for 1 h is required when storage relative humidity exceeds 60% because absorbed surface moisture above 0.03 wt% generates parison surface splay and weld-line defects.

    Standard/RegulationTest or ScopeConditionPass Criterion for Fuel Tank Applications
    ASTM D1238Melt flow rate190 °C / 2.16 kg0.60 g/10 min
    ASTM D792Density23 °C0.964 g/cm³
    ASTM D1693 Condition BEnvironmental stress-cracking resistance, 100% Igepal50 °C>1000 h F50
    FMVSS 301 / ECE R34Fire resistance and crash integrityWhole-tank after 40 km/h impactNo leakage; burn-through exceeds OEM specification
    EPA 40 CFR Part 86 / CARB LEV IIIEvaporative permeation40 °C DBL≤0.5 g/day for light-duty fuel system

    The downstream process is sensitive to parison programming; wall-thickness distribution is controlled by a 100-point parison programmer with die-gap feedback, and the accumulator shot capacity is specified at 5–15 kg to avoid barrel residence times beyond 8 min. Cycle times for 40–80 L passenger-car tanks range from 120–180 s. Compliance testing follows FMVSS 301 for crash integrity and fire resistance, ECE R34 for fire resistance in UNECE markets, and EPA 40 CFR Part 86 or CARB LEV III evaporative permeation limits of 0.5 g/day for light-duty fuel systems. Terminal finished components include 40–80 L passenger-car and light-commercial-vehicle fuel tanks, 10–20 L motorcycle fuel tanks, and off-road fuel reservoirs where steel replacement is driven by mass reduction and corrosion resistance.

    Extrusion blow moulding of tight-head 25 L jerrycans and 200 L open-head drums from DMDH-6400 NT 7 is typically performed on single-station or double-station shuttle machines with grooved-feed extruders of 60–90 mm diameter and L/D 24–30. The resin is dry-blended with 2.5–3.5 wt% UV stabilizer concentrate, 0.5–1.5 wt% colour masterbatch, and up to 30 wt% post-industrial regrind; regrind addition beyond this level reduces ASTM D1693 condition B ESCR below the 400 h F50 threshold needed for aggressive solvent packaging. The melt is extruded at 170–200 °C, preblown at 0.05–0.15 MPa, final-blown at 0.6–0.9 MPa, and cooled in aluminium moulds at 8–15 °C. For 200 L drums, clamp force is specified at 400–800 kN and cycle time at 60–120 s. Compliance is assessed under UN Chapter 6.1, 49 CFR 178.509 for US Department of Transportation approval, ADR/RID 6.1 for European land transport, and IMDG Code Chapter 6.1 for marine shipments; stack testing follows the design-type test schedules of UN Chapter 6.1. Terminal products include 20 L/25 L/30 L tight-head jerrycans, 120 L/200 L/220 L open-head drums, and screw-top chemical containers used for paints, solvents, lubricants, water-treatment chemicals, and non-oxidizing hazardous liquids.

    Batch-to-batch variance on production-scale shuttle machines is primarily observed as wall-thickness asymmetry in the pinch-off zone and base corner; die-head centering and parison programming are logged for each shift because variations greater than ±0.3 mm in the base corner reduce drop-test performance under 49 CFR 178.509. When converters run 200 L drums with 30 wt% regrind, the melt flow rate increase is typically less than 0.10 g/10 min under ASTM D1238, but the ESCR drop can be more than 40%; therefore, regrind content is not controlled only by viscosity. Pre-drying at 70 °C for 1 h is recommended when ambient relative humidity exceeds 60%.

    What Occurs When the Parison Programmer Reduces Wall-Thickness Variation Below ±0.2 mm?

    When the parison programmer reduces wall-thickness variation below ±0.2 mm on 1–20 L agricultural chemical containers, the required drop height and permeation margins improve without increasing cap weight. DMDH-6400 NT 7 is processed as the high-density polyethylene skin layer and regrind layer in triple-layer or six-layer coextrusion with polyamide or EVOH barrier. The barrier layer is added at 2.0–5.0 wt% of total wall thickness, tie layers at 1.0–2.0 wt%, ultraviolet stabilizer concentrate at 1.5–2.5 wt%, antistatic masterbatch at 0.5–1.0 wt%, and pigment masterbatch at 0.5–1.5 wt%; post-industrial regrind is typically limited to 25 wt% because retained solvent from barrier-layer regrind can create pinholes during blow-up. Processing is conducted at die temperatures of 180–210 °C, preblow pressures of 0.05–0.10 MPa, final blow pressures of 0.5–0.8 MPa, and mould temperatures of 10–15 °C. Finished containers are leak-tested at 20–40 kPa internal air pressure and undergo stack loading according to UN Chapter 6.1 for dangerous goods packaging. Regulatory requirements include EPA 40 CFR Part 156 container integrity provisions for pesticide products in the United States and the UN Model Regulations for transport of liquid agrochemicals in Packaging Group II or III. Terminal finished products include 1 L, 5 L, 10 L, and 20 L barrier bottles for pesticides, herbicides, fumigants, and plant growth regulators. Sustained melt temperatures above 220 °C degrade barrier-adhesive tie-layer performance and increase the occurrence of delamination in drop testing; therefore, thermal purge cycles are automated to return the head to 190 °C after colour or barrier resin changes.

    Coolant overflow reservoirs, windscreen washer vessels and HVAC ducting

    Under-hood and interior air-management parts blow moulded from DMDH-6400 NT 7 are specified with 0.1–0.3 wt% antioxidant masterbatch, 1.0–3.0 wt% heat stabilizer masterbatch, 2.0–3.0 wt% carbon black masterbatch for ultraviolet resistance, and up to 25 wt% post-industrial regrind when wall-thickness uniformity is within ±0.3 mm. Processing takes place on 60–80 mm shuttle blow-moulding machines with L/D 22–24, melt temperatures of 180–210 °C, mould temperatures of 12–20 °C, and blow pressures of 0.5–0.8 MPa. The critical process window is parison hang-time control; components with long drop lengths above 300 mm require parison programming to avoid bottom-thickness variation that causes burst failure in pressure-cyclic testing. Compliance is evaluated under FMVSS 302 and ISO 3795 for horizontal flame propagation, ISO 188 for accelerated heat ageing at 125 °C, and ISO 16750-4 for thermal cycling and vibration of road-vehicle components. Published long-term thermal-oxidative ageing data for this specific grade in under-hood coolant environments beyond 1000 h at 125 °C is limited; validation on production-scale parts is required before release for high-temperature engine-bay locations. Terminal finished products include 2–7 L windscreen washer reservoirs, 0.5–2 L coolant overflow bottles, and HVAC air ducts with integrated seals and mounting bosses.

    Large non-potable tanks blow moulded from DMDH-6400 NT 7 include 50 L–1000 L vertical storage vessels, dosing tanks, and diesel exhaust fluid containers where environmental stress-cracking resistance against aggressive fluids is the primary specification. The virgin resin is blended with 2.0–3.0 wt% UV stabilizer concentrate, 1.0–2.0 wt% colour masterbatch, and up to 25 wt% clean post-industrial regrind; for diesel exhaust fluid service, converters restrict regrind to 15 wt% and avoid additives containing free copper or zinc salts because of urea solution instability. Accumulator-head blow-moulding machines with 100–150 mm extruders, L/D 24–30, and shot capacities of 5–20 kg are used to maintain parison wall thickness of 3–8 mm. Processing temperatures are 180–210 °C, mould temperatures 10–15 °C, and blow pressures 0.5–0.8 MPa. Post-mould cooling jigs control ovality to ±0.5% of nominal diameter, and tanks are hydrostatically tested at 50–100 kPa for 24 h. Compliance for diesel exhaust fluid storage follows ISO 22241-3 material compatibility recommendations; transport containers for chemical dosing comply with UN Chapter 6.1 when used for regulated liquids. Potable-water contact is not assumed for this grade and must be validated separately under NSF/ANSI 61 or equivalent national certification. Terminal finished products include 50 L, 120 L, 200 L, 500 L, and 1000 L vertical storage tanks, chemical dosing day tanks, and removable 10–50 L DEF top-up reservoirs for agricultural and construction equipment.

    Closed-loop regrind streams in 10–25 L pail blow moulding

    For non-hazardous industrial pails of 10–25 L, DMDH-6400 NT 7 is processed with post-industrial regrind addition up to 40 wt% when ASTM D1693 condition B ESCR remains above 200 h F50 and ISO 180/A notched Izod impact remains above 10 kJ/m². The additive package comprises 1.0–2.0 wt% pigment masterbatch, 0.5–1.0 wt% processing-aid masterbatch, and 0.1–0.3 wt% antioxidant masterbatch. Single-station blow-moulding machines with 60–80 mm extruders, L/D 22–24, and 2–5 kg accumulator heads maintain melt temperatures between 180 °C and 210 °C; mould temperatures are held at 10–18 °C and blow pressure at 0.5–0.8 MPa. Cycle times range from 30–60 s, depending on pail volume and handle type. When pails are used to ship dangerous goods, regrind is reduced to 30 wt% and finished pails are qualified under UN Chapter 6.1 and 49 CFR 178.509 stack and drop protocols; otherwise, pails are validated against ASTM D256 lid-impact and ASTM D1693 ESCR requirements for non-hazardous industrial liquids. Published data for multi-generation closed-loop regrind streams beyond five cycles using this specific grade is limited; converters are advised to monitor melt flow rate drift under ASTM D1238 and not exceed a cumulative shift of 0.10 g/10 min. Terminal finished products include 5 L, 10 L, 20 L, and 25 L pails and buckets for lubricants, inks, coatings, adhesives, and non-food liquid chemicals with tamper-evident lids and wire handles.

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    Certification & Compliance
    More Introduction

    Dow HDPE DMDH-6400 NT 7 is classified as a high-density polyethylene copolymer for extrusion blow molding. The resin is supplied as a natural pellet without carbon black or titanium dioxide pigment; the NT 7 suffix identifies the natural, stabilized form used for self-colored or masterbatch-tinted rigid containers. The nominal density is 0.964 g/cm³ when measured under ASTM D792, and the melt flow rate is 0.70 g/10 min under ASTM D1238 at 190 °C with a 2.16 kg load. Environmental stress crack resistance exceeds 600 h under ASTM D1693 Condition B in 100% Igepal CO-630. Those three values—density, melt flow rate, and ESCR—form the primary control set for container producers because they are rapid proxies for crystallinity, average molecular weight, and resistance to chemically accelerated crack propagation. The product is used in extrusion blow molding of rigid bottles and canisters for household chemicals, detergent concentrates, agricultural adjuvants, and industrial fluids requiring high stack strength and resistance to stress cracking. The grade is not formulated for injection molding, blown film, or pressure pipe. Processors considering food-contact or potable water applications must verify the finished article under applicable regulations such as FDA 21 CFR or EU/10/2011; the standard technical data sheet does not by itself confer food-contact clearance.

    What separates a 0.964 g/cm³ blow molding resin from lower-density HDPE grades?

    DMDH-6400 NT 7 sits in the upper density range for blow molding HDPE. Many general-purpose bottle grades are engineered in the 0.948–0.955 g/cm³ range to preserve squeeze ease and reduce part weight. A density of 0.964 g/cm³ increases the crystalline fraction and raises flexural modulus. The supplied nominal flexural modulus of 1,450 MPa under ASTM D790 is above the 1,100–1,300 MPa class commonly referenced for lower-density HDPE blow molding resins. That increment improves top-load capacity and sidewall stiffness for cylindrical containers that must survive pallet stacking. The trade-off is that higher density normally reduces environmental stress crack resistance. This grade compensates through a high-molecular-weight copolymer architecture that retains an ESCR above 600 h under ASTM D1693. Compared with a fractional-melt HMW-HDPE at 0.30 g/10 min, the 0.70 g/10 min melt flow rate of DMDH-6400 NT 7 reduces extrusion head pressure and allows lower melt temperatures on continuous shuttle machines, but it also reduces parison hang strength slightly. For containers above 10 L, accumulator heads and parison programming become critical to avoid thickness variation. The resin should not be substituted into an injection-grade mold because injection molding grades for pails and caps typically use melt flow rates in the 4–8 g/10 min range; the 0.70 g/10 min flow rate is too low for short injection filling paths.

    Nominal physical and thermal properties of Dow HDPE DMDH-6400 NT 7
    PropertyStandardNominal value
    DensityASTM D7920.964 g/cm³
    Melt flow rate, 190 °C/2.16 kgASTM D12380.70 g/10 min
    Environmental stress crack resistance, 100% Igepal, Condition BASTM D1693>600 h
    Tensile strength at yieldASTM D63830 MPa
    Elongation at breakASTM D638>600%
    Flexural modulusASTM D7901,450 MPa
    HardnessASTM D224068 Shore D
    Vicat softening temperatureASTM D1525127 °C

    Melt temperature control is the narrowest processing constraint for DMDH-6400 NT 7. On a continuous shuttle blow molder with a grooved-feed extruder of 45 mm to 60 mm screw diameter and an L/D ratio of 24:1 to 30:1, the melt temperature measured at the die is typically held between 180 °C and 210 °C. Below 180 °C, melt fracture, pinholing, and poor pinch-off welds become more probable. Above 230 °C, oxidative by-products increase and parison sag disturbs wall thickness control. The low-shear melt flow rate of 0.70 g/10 min does not represent extrusion shear viscosity; a capillary rheometer sweep from 100 s⁻¹ to 1,000 s⁻¹ at 190 °C is recommended for die design and head-pressure prediction. Die land length ratios of 12:1 to 20:1 and a diverging die gap of 0.8 mm to 2.0 mm are typical for HDPE blow molding heads. Narrower gaps increase shear heating and may raise melt temperature at the die lip. When regrind is used at levels above 20%, melt temperature compensation and lower screw speed are usually required to avoid an increase in gel-like defects. Surface moisture from humid plant air above 60% relative humidity can cause splay; a hopper dryer at 65 °C for 2 h is adequate for removing surface condensation. The grooved feed section should be water-cooled, and melt temperature sensors should be located at the die rather than only in the extruder barrel because the die is the point at which parison temperature controls wall thickness and sag.

    When chemical stress cracking governs container service life

    The ESCR value for DMDH-6400 NT 7 is reported as >600 h under ASTM D1693 Condition B with 100% Igepal CO-630 at 50 °C. That test uses a notched, bent specimen at constant strain and ranks ethylene plastics by time to 50% failure. The result is a comparative index, not a direct service-life prediction. Containers for detergents, wetting agents, and diluted agricultural chemicals benefit from this ESCR level, but field failures are controlled by molded-in stress at the pinch-off, handle welds, and closure shoulder. Stress concentrations in the weld region can reduce time to crack initiation even when the base resin passes the standardized test. The resin is not recommended for continuous contact with aromatic hydrocarbon solvents, chlorinated solvents, or concentrated strong oxidizers. Methylene chloride, toluene, and xylene can swell the surface, while oxidizing acids accelerate surface embrittlement. For aggressive formulations, storage stability tests with the finished bottle and closure torque are required under end-use conditions. Alcohol-based formulations should be evaluated at elevated temperatures because environmental stress cracking in HDPE can occur at lower strain when the specimen is notched. Molded-in stress from low mold temperatures or excessive injection pressure during parison inflation should be treated as a compounding variable that can shorten service life even when the resin ESCR is above 600 h.

    Top-load performance, wall thickness distribution, and tooling constraints

    For a cylindrical container with wall thickness between 0.6 mm and 1.0 mm, the flexural modulus of 1,450 MPa under ASTM D790 contributes to high top-load capacity, but top-load failure is dominated by buckling and shoulder ovalization rather than by pure compressive yield. Blow molds for DMDH-6400 NT 7 should maintain a pinch-off land length of 0.3–0.5 mm per side and a mold temperature between 10 °C and 25 °C for surface gloss and dimensional stability. Lower mold temperatures increase residual stress and reduce ESCR at the pinch-off. A 64-point parison programmer is recommended for consistent wall distribution; shoulder regions typically require a 20% to 30% increase in die gap relative to the sidewall to offset draw-down and maintain minimum thickness. Pre-colored grades with carbon black or titanium dioxide differ from this natural grade. Carbon black adds outdoor weathering stability, while natural resin may require a UV stabilizer masterbatch for prolonged outdoor storage. The natural pellet form permits dry blending with polyolefin-carrier masterbatches; incompatible carriers can reduce weld strength and should be avoided. Color masterbatch additions should be validated for ESCR retention because some low-molecular-weight color carriers migrate to the surface and lower stress crack resistance.

    Detailed molecular weight distribution data and comonomer type are not specified on the standard product data sheet. Processors requiring those values should request a certificate of analysis or discuss gel permeation chromatography and crystallization elution fractionation data with the supplier. Incoming inspection should record density and melt flow rate because these are the two most commonly supplied lot-control values. Regulatory status must be verified through the current supplier safety data sheet and regulatory certificate. The product is a natural, stabilized HDPE; it does not contain intentionally added carbon black or titanium dioxide. Processors must confirm compliance with REACH and RoHS for the manufactured article, and no food-contact or potable water approval is implied by the physical property data. Because the material is not designed for medical use, implant or parenteral applications are outside the stated use range.

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