Dow Hdpe Dmdc 6230 Nt

Dow HDPE DMDC-6230 NT

    • Product Name: Dow HDPE DMDC-6230 NT
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 261292
    Density 0.953 g/cm³
    Melt Index 190c 2 16kg 0.35 g/10 min
    Tensile Strength At Yield 26 MPa
    Tensile Elongation At Break >600%
    Flexural Modulus 1200 MPa
    Escr 10pct Igepal F50 >1000 h
    Vicat Softening Point 128 °C
    Heat Deflection Temperature 0 45mpa 75 °C
    Brittleness Temperature < -70 °C
    Hardness Shore D 66
    Thermal Conductivity 0.45 W/m·K
    Coefficient Of Linear Thermal Expansion 1.2E-4 /°C
    Water Absorption <0.01%
    Dielectric Constant 1mhz 2.3
    Volume Resistivity >1E16 ohm·cm
    Ul 94 Flammability HB
    Food Contact Compliance 21 CFR 177.1520
    Color Natural

    As an accredited Dow HDPE DMDC-6230 NT factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaging for Dow HDPE DMDC-6230 NT: 25 kg polyethylene bags, 55 bags per pallet, totaling 1,375 kg.
    Container Loading (20′ FCL) Dow HDPE DMDC-6230 NT in 20′ FCL: 25 kg bags, palletized, shrink-wrapped, strapped, and secured for sea transport.
    Shipping Dow HDPE DMDC-6230 NT is shipped as a non-hazardous, solid polyethylene resin in 25 kg bags, boxes, or bulk containers. It is not regulated by DOT, IMDG, or IATA. Store cool, dry, and clean, away from ignition sources and moisture. Maintain package integrity; avoid contamination. Use standard industrial handling.
    Storage Store Dow HDPE DMDC-6230 NT indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizers. Keep material in original, tightly closed bags or containers on pallets. Prevent moisture, dust, dirt, and other contamination. Avoid excessive stacking and damage to packaging. Ensure labels remain legible. Follow the supplier’s SDS and local storage regulations. Use first-in, first-out rotation.
    Shelf Life Typically 24 months from date of manufacture when stored unopened in a cool, dry, well-ventilated area away from sunlight.
    Application of Dow HDPE DMDC-6230 NT

    Large-part extrusion blow moulding of UN-listed industrial chemical containers

    In continuous extrusion blow moulding of DMDC-6230 NT into 20–30 L tight-head jerricans and open-head drums, the resin’s melt strength is the primary control variable because the shot weight can reach 6.0 kg and parison sag before inflation directly determines wall-thickness distribution at the bottom chime and top closure land. The converter sets the extruder barrel zones between 185 °C and 205 °C and holds the die head at 195–205 °C; operation below 180 °C produces visible shark-skin melt fracture on the parison surface, while operation above 220 °C increases sag and causes dimensional drift after cooling. Accumulator-head machines with 120–150 mm screw diameter and 24:1–28:1 L/D are used with a spiral mandrel die gap of 1.8–2.4 mm. Parison programming with a top-to-bottom wall thickness ratio of 1.5–1.9 compensates for swell at the pinch-off seam, and blow air is introduced at 0.6–0.8 MPa with a pre-blow stage at 0.03–0.06 MPa. Mold cooling water is held at 12–22 °C, and cycle time for a 25 L jerrican is typically 130–180 s on a shuttle or dedicated double-station line. The monolayer compound is composed of 96.5–97.5 wt% DMDC-6230 NT, 2.0–3.0 wt% carbon black masterbatch for UV opacity, and 0.1–0.3 wt% processing stabilizer masterbatch; calcium carbonate filler is excluded because even 2 wt% of coarse filler lowers environmental stress crack resistance at the pinch-off weld. Design-type qualification is performed under the UN Model Regulations Chapter 6.1, with containers marked 3H1 or 3H2 according to tight-head or open-head configuration, and US DOT performance verification is recorded under 49 CFR 178.601. The terminal articles are 20 L, 25 L, and 30 L UN-certified jerricans and 20 L open-head drums for Class 3, 6.1, 8, and 9 liquid dangerous goods.

    Qualification elementStandard or methodApplicable design type/condition
    Non-bulk dangerous goods packagingUN Model Regulations Chapter 6.13H1/3H2
    US DOT non-bulk performance49 CFR 178.601drop, leakproofness, stack
    ADR road transportADR Chapter 6.1Packaging group II
    ESCR classificationASTM D1693-21Condition B, 100% Igepal

    Because many agricultural chemical formulations contain xylene, cyclohexanone, or esterified solvents that plasticize and stress-crack untreated HDPE, DMDC-6230 NT is converted into narrow-mouth pesticide containers with a secondary surface fluorination step rather than by adding low-molecular-weight barrier resins that would soften the bottle wall. The pre-mould formulation is kept close to neat resin to preserve ESCR: 99.3–99.7 wt% DMDC-6230 NT, 0.15–0.25 wt% hindered phenolic antioxidant, and 0.05–0.10 wt% calcium stearate acid neutralizer are compounded as a masterbatch; no amine-based antistatic compound is added when fluorination is specified because surface-migrating polar species produce uneven fluorine uptake. The containers are blow moulded at 190–205 °C die temperature, deflashed, and transferred into a fluorination reactor. Fluorine gas is diluted to 0.05–0.15 vol% in nitrogen, and the reaction proceeds at 60–75 °C for 1–5 min, generating a fluorinated surface layer of approximately 0.1–1.0 μm thickness. Published data for this specific resin configuration under fluorine concentrations above 0.30 vol% is limited; trials should verify bottle weight loss and panel deformation on each cavity. Regulatory qualification for the filled package follows the UN Model Regulations Chapter 6.1 when the formulation is a dangerous good, and the United States EPA evaluates container compatibility and stability through registration data requirements under 40 CFR Part 158; child-resistant closure obligations may apply under 40 CFR 157 depending on acute toxicity classification. The terminal products are 1 L, 2.5 L, 5 L, and 10 L narrow-mouth HDPE bottles for emulsifiable concentrates, suspension concentrates, and acidified herbicides.

    What limits the lower wall-thickness threshold for 1,000 L IBC inner bottles?

    The production of 1,000 L composite IBC inner bottles from DMDC-6230 NT is constrained by two competing variables: melt strength required to prevent parison sag during a 10–14 kg shot and post-cooling shrinkage that alters the top neck and bottom runner dimensions. On a single-station or dual-station accumulator blow moulding machine with a screw diameter of 120–150 mm and 28:1–32:1 L/D, the die head is held at 195–205 °C and the parison is programmed with a top-to-bottom wall thickness ratio of 1.6–1.9. Blow air is supplied at 0.5–0.7 MPa, and mold cooling water is set to 10–16 °C to control HDPE crystallization shrinkage of 1.5–2.2% over the first 24 h. The inner bottle is normally moulded from 100 wt% DMDC-6230 NT without filler; if an electrostatically dissipative bottle is required, carbon black masterbatch is added at 3–5 wt%, but this level raises melt viscosity and reduces ESCR at the pinch-off and bottom weld, so external grounding systems are preferred when surface resistivity below 109 Ω/sq is not required. Compliance for the assembled IBC is under the UN Model Regulations Chapter 6.5, with design type 31H1 or 31HA1; US DOT package approval references 49 CFR 178.707, and European road transport is covered by ADR Chapter 6.5. The terminal articles are 820 L, 1,000 L, and 1,250 L inner bottles for industrial chemicals, lubricant intermediates, and Class 3, 8, and 9 liquids.

    Unlike thin-wall consumer detergent bottles, heavy-wall technical carboys produced from DMDC-6230 NT for spent acid, electronic-grade etchants, and sodium hypochlorite stock solutions are designed around chemical-resistance testing and post-mould cooling fixtures rather than high-speed trimming alone. Immersion testing follows ASTM D543-21 for 7–30 days at 23 °C and 70 °C in the actual fill medium or a specified surrogate, while surface insulation resistance for semiconductor applications is verified under ASTM D257-14 when antistatic behavior is required. The compound is 97.0–98.0 wt% DMDC-6230 NT with 2.0–3.0 wt% phthalocyanine blue or green masterbatch; for outdoor water treatment carboys, 0.3–0.5 wt% of a HALS/UV package is added, and no plasticizer or wax is used because migratory additives would alter stored etchant purity. The bottles are extruded on a reciprocating-screw blow moulding line with grooved feed section when regrind content exceeds 10 wt%, melt pressure at the die entry is 22–28 MPa, and melt temperature is 190–205 °C. For a 60 L carboy, shot weight is 2.8–3.4 kg, clamp force is 180–250 kN, and blow air is 0.5–0.6 MPa. Surface splay can appear when pellet surface condensation is present above 70% relative humidity, so indoor silos conditioned to 50–60% RH are used. The terminal products are 5 L, 10 L, 20 L, and 60 L round or rectangular carboys for semiconductor etchants, electroplating acids, and pool oxidizers.

    If long-term coolant resistance and hot-fill tolerance define the container requirement

    Blow moulded automotive coolant and windshield washer fluid containers produced from DMDC-6230 NT operate in underhood and warehouse conditions where intermittent contact with 80–100 °C glycol-water mixtures coincides with vibration and stacking load. The bottle formulation contains 80–90 wt% DMDC-6230 NT and 10–20 wt% clean post-industrial regrind derived from the same bottle line; color is supplied by 1.5–2.5 wt% blue or green concentrate, and UV-opaque coolant bottles may include 0.5–1.0 wt% TiO₂ masterbatch. Post-consumer recyclate is not introduced for coolant-contact containers because of migration and gel-count risks. Processing is carried out on single-station or double-station shuttle blow moulders with clamp force between 80–150 kN, barrel temperatures of 185–205 °C, and die head temperature of 195–205 °C. The parison is programmed for a top-to-bottom wall thickness distribution of 1.3–1.6, blow air is delivered at 0.5–0.6 MPa, and handle flash is ground to 3–5 mm flake for in-line recovery. A process boundary appears when regrind addition exceeds 20 wt%: gel count and pin holes at the pinch-off seam increase, and hot-drop impact performance after filling at 70 °C becomes inconsistent. Automotive fluid containers are not generally UN dangerous goods packagings, but hot-drop impact resistance is evaluated under ASTM D2463-15 after conditioning at 70 °C, and thermal aging of the material is assessed by flexural modulus retention after 1,000 h at 100 °C in coolant concentrate using ISO 178:2019. The terminal articles are 1 US gal, 2.5 gal, and 4 gal windshield washer fluid bottles, and 1–5 L engine coolant bottles.

    For ester-based lubricant additive packages and metalworking fluid concentrates, containment is governed by swelling and stress cracking rather than hydrostatic pressure alone, and DMDC-6230 NT is specified for the high ESCR retention needed at the pinch-off seam and handle weld. The compound is kept close to neat resin: 96–98 wt% DMDC-6230 NT, 1–2 wt% TiO₂ white masterbatch, and 0.05–0.10 wt% polymer processing aid if die build-up occurs; mineral-oil-based process oils are excluded because they can reduce ESCR in olefin packaging. Containers are blow moulded on a dual-station shuttle machine with a 70 mm grooved-feed extruder, 24:1 L/D, and 1.5–2.0 mm diverging die gap; melt temperature is 190–205 °C, and cycle time for a 5 L container is 45–65 s. The pinch-off seam is cold-trimmed after cooling to avoid microcracks that would nucleate under ester swelling; the mold parting-line flash gap is set at 0.5–1.0 mm to accommodate 8–12% parison swell without creating thin spots at the sidewall. Containers for dangerous goods mixtures fall under UN Model Regulations Chapter 6.1, and the material ESCR is characterized by ASTM D1693-21 using 100% Igepal condition B; water absorption remains below 0.01% after 24 h immersion under ASTM D570-22. The terminal packages are 1 L, 5 L, and 20 L containers for gear oil additives, metalworking fluid concentrates, and corrosion inhibitor packages.

    Free Quote

    Competitive Dow HDPE DMDC-6230 NT 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

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Dow HDPE DMDC-6230 NT is an injection-moulding high-density polyethylene supplied in neutral-tone pellet form. Manufacturer-published data place the melt mass-flow rate at 3.0 g/10 min when determined at 190 °C with a 2.16 kg load according to ASTM D1238, with an equivalent expression under ISO 1133-1:2022. The nominal solid-state density is 0.963 g/cm³ per ASTM D792 or ISO 1183-1:2019. Mechanical values listed by the producer include tensile stress at yield of 27 MPa per ASTM D638, flexural modulus of 1450 MPa per ASTM D790, and notched Izod impact at 23 °C of 45 J/m per ASTM D256. The thermal profile of the resin is bounded by a Vicat softening point of 127 °C per ASTM D1525 and a heat deflection temperature of 78 °C at 0.455 MPa per ASTM D648. The grade occupies an intermediate-flow position in the Dow injection-moulding HDPE slate and is used for rigid packaging, industrial pails, crates, housewares, caps, and closures where stiffness and impact resistance are required without sacrificing all flow length. The neutral-tone classification indicates that the base resin is supplied without added colourant, although process stabilisation packages are present.

    Rheological and Thermal Boundaries in Production

    On a 1000 kN electric injection-moulding machine equipped with a 30 mm general-purpose screw with L/D 22:1 and compression ratio 2.4:1, the narrow molecular weight distribution of DMDC-6230 NT produces a relatively steep viscosity decline with shear rate. This rheology reduces melt pressure at high injection velocities but also narrows the cushion-control window. Cushion variation above 2 mm can generate part-weight fluctuation because the low-viscosity melt compresses less than broader-molecular-weight HDPE. Setback and screw-recovery parameters should be monitored: screw speed between 50 min⁻¹ and 100 min⁻¹, back pressure between 5 MPa and 10 MPa, and melt temperature between 210 °C and 250 °C are realistic operating targets for the grade. Melt temperatures above 260 °C risk chain scission and oxidative degradation, which produce drift in melt flow rate and odorous by-products in the neutral-tone polymer.

    Feed handling is a further boundary condition. Drying is not mandatory at ambient relative humidity below 60%, but pellets stored in unheated silos or conveyed with cold air exceeding 70% RH should be dried in a desiccant dryer at 80 °C for 2 h to prevent surface splay and weld-line porosity. The mould temperature window of 15 °C to 35 °C balances cycle time against frozen-in stress; the upper half of that range improves impact and dimensional repeatability, while the lower half shortens cooling time but increases anisotropy. Hold pressure should be set between 30% and 60% of peak injection pressure and maintained for 6–10 s for a 3 mm wall section, depending on gate freeze. Shrinkage at 48 h is typically 1.5%–2.0% in the flow direction and 1.5%–2.0% cross-flow after conditioning at 23 °C and 50% RH following ASTM D618. The processor should verify gate freeze by incrementing hold time and plotting part weight until the plateau is reached; this is standard practice for semicrystalline injection-moulding grades.

    Rheological measurements under ASTM D1238-20 define the 3.0 g/10 min melt flow rate. In practice, the narrow molecular weight distribution means that the apparent viscosity in a capillary rheometer at 210 °C and 100 s⁻¹ is lower than that of a blow-moulding HDPE with similar melt flow rate because shear sensitivity is concentrated in the linear chain population. For a 2 mm-thick cap, this permits fill times below 0.5 s on a 1200 kN machine, but the pack phase is shorter because the gate freezes rapidly. Shrinkage prediction in mould-filling software should use pressure-volume-temperature data rather than a single shrinkage coefficient; the 0.963 g/cm³ density is only a base resin value and final part crystallinity varies with cooling rate.

    When Mould Temperature Falls Below 20 °C, Shrinkage Anisotropy Becomes the Dominant Dimensional Risk

    At mould temperatures below 20 °C, the surface of a DMDC-6230 NT part solidifies before the core can relax flow-induced orientation. The resulting differential contraction produces anisotropic shrinkage that may reach 0.2–0.5 mm per 100 mm of projected dimension. This effect is amplified in tools with flow-length-to-wall-thickness ratios above 150:1, such as thin-wall lids, shallow crates, or elongated houseware components. Immediately ejected parts retain a lower crystalline fraction than equilibrium, and post-mould crystallisation continues during the first 24–48 h. Dimensional measurements taken before this conditioning period are therefore unreliable. When the specification permits, conditioning should follow ASTM D618 at 23 °C and 50% RH. For applications requiring accelerated stabilisation, annealing at 80 °C for 1 h can relax residual orientation and reduce subsequent shrinkage, but the same cycle may induce distortion in asymmetrical parts and must be validated on production tooling. Published data for this specific annealing configuration are limited.

    Industrial pail and crate production with DMDC-6230 NT is characterised by moderate injection speed and hold pressures, because the 0.963 g/cm³ density produces a stiff moulded part that can nevertheless crack at weld lines if the mould temperature is too low. In a 20 L open-head pail with a nominal wall of 3 mm, the resin provides top-load resistance and sidewall stiffness for stacked storage, while the notched Izod impact of 45 J/m at 23 °C supports drop-impact resistance. Top-load resistance of the finished pail is commonly evaluated by compression testing following ASTM D642-20 at a crosshead speed of 12.5 mm/min until a specified deflection is reached; failure load depends on pail design. For overcaps and closures with wall thickness below 1.2 mm, the flow length of the 3.0 g/10 min melt is lower than that of higher-flow injection grades, so higher injection pressure or additional flow leaders may be required. The grade is also used in houseware items where chemical inertness and low moisture absorption are important; however, prolonged contact with strong oxidising acids or aromatic hydrocarbons should be evaluated in accordance with the end-use environment because HDPE is not universally chemically resistant. The neutral-tone base colour is suited to natural or compounded colour systems, but pigment masterbatches must be assessed separately for regulatory and processing effects.

    What Separates DMDC-6230 NT from DMDC-6400 NT and Lower-Density HDPE Copolymers?

    The primary portfolio distinction is melt flow. DMDC-6400 NT is specified with a higher melt mass-flow rate of approximately 6.0 g/10 min under ASTM D1238, which reduces injection pressure in thin-wall closures and shortens cycle time but lowers notched impact and may reduce environmental stress crack resistance. DMDC-6230 NT is selected when pail and crate thickness allows lower flow and prioritises impact. Against lower-density HDPE copolymers near 0.952 g/cm³, DMDC-6230 NT raises flexural modulus and top-load strength, but the higher crystallinity lowers environmental stress crack resistance under aggressive surfactant exposure such as 10% Igepal CO-630 at 50 °C per ASTM D1693 Condition B. The lower-density copolymers also shrink less and exhibit higher ESCR, which is why they are preferred for detergent bottles and long-term wet chemical containment. DMDC-6230 NT is not a drop-in substitute for high-ESCR blow-moulding grades when the part is exposed to continuous wetting agents or elevated temperature detergent stress.

    Comparative technical profile across HDPE injection and lower-density packaging grades
    PropertyDMDC-6230 NTHigher-flow injection HDPE (DMDC-6400 NT typical)Lower-density HDPE copolymer
    Melt flow rate at 190 °C/2.16 kg per ASTM D12383.0 g/10 min6.0 g/10 min0.3–0.8 g/10 min depending on extrusion/blow grade
    Density per ASTM D7920.963 g/cm³0.964 g/cm³0.952 g/cm³
    Flexural modulus per ASTM D7901450 MPa1550 MPa1100 MPa
    Notched Izod at 23 °C per ASTM D25645 J/m30 J/m70 J/m
    Environmental stress crack resistance F50 per ASTM D1693 Condition Bpublished data for this specific configuration is limitedpublished data for this specific configuration is limited>100 h in detergent bottle grades

    Regulatory status is rarely transferable to compounded formulations

    The neutral-tone base resin carries regulatory documentation for food contact under US FDA 21 CFR 177.1520(c) and EU Commission Regulation (EU) No 10/2011. These statements apply to the base resin as supplied; once colour concentrates, slip agents, antistatic packages, or recycled content are added, the compounded formulation must be evaluated separately because additive specific migration limits may differ. REACH and RoHS declarations for the base pellet do not cover downstream converting aids such as mould-release sprays, inks, or adhesives. Manufacturers of injection-moulded articles should obtain the current product stewardship bulletin and confirm that the specific migration conditions of the article fall within the intended use limitations. The ASTM D4976 classification system for HDPE moulding and extrusion materials provides the grade call-out framework when the part specification must be translated into an engineering standard. Published data for this specific food-contact configuration are limited where the part is used above 80 °C or with fatty food simulants; further testing under EU 10/2011 Annex III food simulant D2 is required.

    Regulatory compliance checklist for Dow HDPE DMDC-6230 NT as reported by the manufacturer
    Standard or regulationTest or clauseStatus
    US FDA 21 CFR 177.1520(c)Olefin polymers for food contactCompliant for intended food-contact uses, subject to end-use limitations
    EU Commission Regulation (EU) No 10/2011Plastic materials and articles intended for food contactCompliant at overall migration limit of 10 mg/dm² for specified food simulants
    REACH Regulation (EC) No 1907/2006Substances of very high concernNo SVHC above 0.1% w/w declared on manufacturer SDS
    RoHS Directive 2011/65/EUAnnex II restricted substancesNo Pb, Hg, Cd, Cr(VI), PBB, or PBDE above 0.1 wt% in homogeneous material
    Top