Dow Hdpe Dmdj 6200

Dow HDPE DMDJ-6200

    • Product Name: Dow HDPE DMDJ-6200
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 680459
    Density 0.962 g/cm3
    Meltindex 0.35 g/10 min (190°C/2.16 kg)
    Meltingpoint 134 °C
    Vicatsofteningtemperature 127 °C
    Heatdeflectiontemperature 74 °C at 0.45 MPa
    Tensilestrengthatyield 27 MPa
    Tensilestrengthatbreak 31 MPa
    Elongationatbreak 600%
    Flexuralmodulus 1200 MPa
    Environmentalstresscrackresistance >1000 h (10% Igepal, Condition A)
    Hardnessshored 66
    Thermalconductivity 0.36 W/m·K
    Coefficientoflinearthermalexpansion 1.2E-4 /°C
    Specificheatcapacity 1.9 kJ/kg·K
    Waterabsorption <0.01%

    As an accredited Dow HDPE DMDJ-6200 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Dow HDPE DMDJ-6200 is packaged in 25 kg polyethylene bags, with 55 bags per pallet (1,375 kg total).
    Container Loading (20′ FCL) Container Loading (20′ FCL) for Dow HDPE DMDJ-6200: 25 kg bags, palletized or floor-loaded, shrink-wrapped, secured; typical 18–20 MT net.
    Shipping Dow HDPE DMDJ-6200 is shipped as non-hazardous polyethylene resin pellets in moisture-resistant 25 kg bags or bulk containers, palletized and stretch-wrapped. Transport in clean, dry vehicles at ambient temperature; avoid direct sunlight, heat, and contamination. No UN hazard class or special transport placards required.
    Storage Store Dow HDPE DMDJ-6200 in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and strong oxidizers. Keep material in original sealed packaging on pallets, off the floor, to prevent contamination and water absorption. Avoid prolonged UV exposure. Maintain moderate temperatures and practice first-in, first-out stock rotation. Follow the supplier’s SDS and local regulations.
    Shelf Life Dow HDPE DMDJ-6200 has no defined shelf life under recommended storage conditions; keep cool, dry, and away from direct sunlight.
    Application of Dow HDPE DMDJ-6200

    Extrusion blow moulding of UN-type 3H1 jerrycans with DMDJ-6200 is specified where design type approval under UN Model Regulations Chapter 6.1, ADR 6.1, and IMDG Code 6.1 is mandatory for liquid dangerous goods. The grade’s melt flow rate of 0.60 g/10 min at 190°C/2.16 kg per ISO 1133-1:2022 and density of 0.962 g/cm³ per ISO 1183-1:2019 provide parison strength sufficient for accumulator-head machines producing containers from 5 L to 25 L without radial wall collapse. A monolayer formulation applied in production-scale lines contains 95–98 wt% virgin DMDJ-6200, 1–3 wt% UV-stabilized color concentrate, 0.1–0.5 wt% hindered amine light stabilizer when outdoor exposure is required, and 0.02–0.1 wt% processing aid. Clean flash regrind is limited to 20 wt% because higher fractions reduce environmental stress-crack resistance measured under ASTM D1693-15 condition B, with F50 values falling below 600 h in 100% Igepal CO-630 at 50°C. Processing on shuttle or accumulator blow moulders with 60–80 mm grooved-feed extruders and L/D 24:1–30:1 uses barrel temperature settings of 180–210°C, die head settings of 190–205°C, and mould temperature settings of 8–25°C; parison programming controls wall thickness between 1.5 mm and 3.0 mm, while blow air is held at 0.6–0.8 MPa. Finished article types include 5 L, 10 L, 20 L, and 25 L tight-head jerrycans marked UN 3H1/Y with injection-moulded closures and EPDM or PE-foam gaskets. Post-mould leak testing at 20 kPa and hydraulic proof testing at 100 kPa for Packing Group II are applied before batch release.

    Rigid plastics jerrican design type test matrix applied to DMDJ-6200 dangerous goods containers under UN Model Regulations Chapter 6.1
    UN packing groupDrop height at relative density ≤1.2Hydraulic test pressureLeakproofness test pressure
    I1.8 m250 kPa20 kPa
    II1.2 m100 kPa20 kPa
    III0.8 m100 kPa20 kPa

    Why Is Six-Layer Coextrusion Blow Moulding Preferred for Agrochemical Emulsifiable Concentrates?

    For solvent-based pesticide and agrochemical formulations, DMDJ-6200 is used in coextrusion blow moulding as the outer skin, inner skin, and regrind carrier with a central ethylene-vinyl alcohol copolymer barrier. The relevant packaging regulations include UN Model Regulations Chapter 6.1, ADR 6.1 for road transport, IMDG Code 6.1 for sea freight, and US 40 CFR Part 165 for agricultural pesticide container design and residue removal. A six-layer construction for a 1 L emulsifiable concentrate bottle typically combines 40–60 wt% DMDJ-6200 across outer, inner, and regrind layers, 3–6 wt% EVOH barrier resin, 1–3 wt% adhesive tie resin, 1–2 wt% color and UV masterbatch, and 20–40 wt% clean post-consumer HDPE where brand specifications permit. The conversion line uses separate extruders for each layer, with DMDJ-6200 cylindrical screw temperatures of 180–210°C, tie-layer temperatures of 200–215°C, and EVOH temperatures maintained below 220°C to avoid gel formation. Spiral mandrel die heads and parison programming control total wall thickness from 0.8 mm to 2.0 mm, with an asymmetric layer distribution that places the barrier toward the package interior to maximize solvent barrier performance. Because EVOH thermal degradation forms cross-linked gels above 220°C, the coextrusion feedblock must be purged with HDPE before shutdown; DMDJ-6200 serves as purge resin because its viscosity matches the adhesive and barrier melt streams. Layer thickness ratios are adjusted by gear pump outputs, not by screw speed alone, to maintain barrier layer thickness at 5–8% of total wall thickness. Containers are blow moulded at 0.6–0.8 MPa blow air and mould temperatures of 8–20°C, then de-flashed, leak-tested, and subjected to UN design type drop and hydraulic pressure protocols. Terminal articles include 500 mL, 1 L, 5 L, and 20 L tight-head agrochemical bottles and jerrycans for xylene-, cyclohexanone-, and ester-based emulsifiable concentrates. Published data for long-term solvent weight loss through this specific DMDJ-6200/EVOH layer stack is limited; qualification therefore requires solvent immersion testing at 40°C for 28 days according to the packer’s internal protocol.

    Detergent bottle manufacturing with DMDJ-6200 is concentrated on shuttle blow moulding lines producing high-top-load containers for sodium hypochlorite, quaternary ammonium disinfectants, and linear alkylbenzene sulfonate-based cleaners. EU regulatory compliance for the finished package is defined under Regulation (EC) No 648/2004 for detergent labelling and REACH (EC) No 1907/2006 Annex XVII for restricted substances, while US closures fall under 16 CFR 1500 for household product packaging. A typical monolayer formulation uses 97–99 wt% DMDJ-6200, 1–2 wt% color masterbatch, and 0.05–0.1 wt% slip/antiblock concentrate; clean in-house regrind is added up to 20 wt% without filler because calcium carbonate additions above 2 wt% lower tensile yield below 30 MPa and reduce top-load under ISO 12048:2001. Melt conversion is performed on 50–75 mm extruders with L/D 24:1–28:1, barrel temperatures of 180–210°C, and mould temperatures of 10–20°C; parison wall thickness is set from 0.5 mm to 1.5 mm depending on bottle volume. Post-mould flash is granulated through 100–200 µm screen packs and redirected into the main feed. Pressure-decay leak detection at 5–10 kPa is applied before filling. Finished product types include 500 mL trigger spray bottles, 1 L and 2 L laundry detergent bottles, 5 L household cleaner jugs, and 20 L industrial cleaning canisters that are not subject to UN dangerous goods marking when formulations are non-hazardous. A limitation for bleach packaging is that prolonged storage above 40°C accelerates oxidative stress cracking; therefore closure torque and top-load retention should be validated under ASTM D2659-16 and ISO 8317:2015 where child-resistant closures are required.

    Dimensional Stability and Hot-Plate Weld Integrity in Automotive Auxiliary Fluid Reservoirs

    DMDJ-6200 is converted into automotive windshield washer fluid reservoirs, coolant expansion tanks, and headlamp washer containers where low-temperature impact resistance and dimensional stability after welding are required. Material compliance is evaluated against ISO 16750-3:2012 for vibration and temperature cycling, EU ELV 2000/53/EC for restricted substances, and REACH Annex XVII; OEM approvals frequently add odour and fogging limits under VDA 270:2018. The formulation on production-scale lines contains 90–97 wt% DMDJ-6200, 2–3 wt% carbon black masterbatch for UV stability, 0.1–0.2 wt% hindered phenolic antioxidant, and 0.02–0.1 wt% processing aid; PCR content up to 20 wt% is used only when the OEM specification approves recycled feedstock. Extrusion blow moulding is performed on accumulator-head machines with 3D parison manipulation for complex underhood shapes, wall thickness from 2.0 mm to 3.5 mm, barrel temperatures of 180–210°C, and mould temperatures of 8–15°C to control post-mould shrinkage at 1.5–2.0% after 24 h at 23°C. Hot-plate welding of fittings, inlet necks, and bracket bosses uses plate temperatures of 200–220°C and weld pressure of 0.1–0.3 MPa; burst testing is performed at 150 kPa or to the OEM-specific protocol. Plate temperatures above 220°C cause oxidative degradation of the HDPE weld bead, while plate temperatures below 190°C reduce weld strength below burst-test specification. Finished parts include 2–5 L windshield washer reservoirs, coolant expansion tanks, and auxiliary fluid containers rated for continuous use from −40°C to 80°C. The grade is not recommended for underhood components containing anhydrous ammonia or continuous immersion in diesel fuel due to permeation and environmental stress-cracking risk.

    When Cosmetic and Personal Care Bottles Require Stress-Crack Resistance Without Sacrificing Surface Gloss

    DMDJ-6200 is selected for extrusion blow moulded personal care and cosmetic packaging when formulations contain ester-based emollients, mild surfactant systems, or alcohol up to 30 vol%, which can initiate environmental stress cracking in lower-molecular-weight HDPE. The regulatory boundary for finished packaging includes EU Regulation (EC) No 1223/2009 for cosmetic products and 16 CFR 1500 in the United States for consumer packaging safety; material conformity is verified under REACH (EC) No 1907/2006 and, for exported articles, under national packaging contact schemes. A production formulation for glossy containers uses 96–99 wt% DMDJ-6200, 1–3 wt% color masterbatch, and 0.05–0.1 wt% antistatic/slip concentrate; fillers are excluded because surface gloss measured under ASTM D523-14 at 60° declines when inert mineral loadings exceed 1 wt%. Extrusion blow moulding is run on single-station machines with vertical plastification and parison length control, barrel temperatures of 180–210°C, mould temperatures of 10–25°C, and cooling air at 0.5–0.7 MPa. For label adhesion, flame treatment is adjusted until wetting tension exceeds 38 mN/m by ASTM D2578-23. Terminal items include 50 mL, 100 mL, 250 mL, 500 mL, and 1 L bottles for shampoos, conditioners, body washes, and body lotions. When high concentrations of isopropyl myristate or ethanol above 30 vol% are specified, the finished container must undergo filled-package stress-crack testing at 40°C for 28 days; published data for this specific DMDJ-6200 formulation is limited beyond the standard ESCR dataset under ASTM D1693-15.

    Closed-Loop Water Storage Containers Require a Virgin Skin Layer Around the Recycled Core

    Returnable water storage containers and closed-loop distribution jerrycans are coextrusion blow moulded with a virgin DMDJ-6200 outer and inner skin surrounding a post-consumer recycled HDPE core. Potable water contact conformity is not a resin-level property and must be established on the finished article under EU Regulation (EC) No 1935/2004, EU Directive (EU) 2020/2184 for drinking water quality, and national schemes such as WRAS BS 6920-1:2014 or NSF/ANSI 61 where the destination market requires certification. The three-layer structure uses 70–80 wt% DMDJ-6200 across the skins, 20–30 wt% post-consumer HDPE in the core, 0.5–1 wt% blue water-contact masterbatch, and 0.1–0.2 wt% hindered phenolic antioxidant; filler and impact modifiers are omitted to maintain tensile yield above 30 MPa. Production is performed on three-layer coextrusion blow moulding machines with 50–70 mm skin extruders and a 35–50 mm core extruder, barrel temperatures of 180–210°C, die head temperatures of 190–205°C, and mould temperatures of 8–20°C. Wall thickness is held at 1.2–2.5 mm, and containers are de-flashed, leak-tested at 20 kPa, and washed closed-loop. Finished products include 5 L, 10 L, and 20 L potable water containers, dispenser bottles, and returnable logistics jerrycans. Continuous hot-fill service above 60°C is outside the recommended processing envelope because creep and top-load retention after the third return cycle must be validated by ISO 12048:2001.

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    Certification & Compliance
    More Introduction

    Dow HDPE DMDJ-6200 is a medium-to-high molecular weight high-density polyethylene homopolymer supplied in natural pellet form under the designation DMDJ-6200 NT 7. The grade is classified for extrusion blow molding of rigid containers in household chemical, pharmaceutical, and industrial packaging applications where melt strength, container stiffness, and environmental stress-crack resistance are jointly specified. The nominal density is 0.956 g/cm³ when measured according to ASTM D1505-18, and the melt flow rate is 0.60 g/10 min under 190 °C and 2.16 kg load according to ASTM D1238-20. These values place DMDJ-6200 between injection-molding HDPE grades with much higher flow and fractional-melt HDPE grades intended for very large containers or extended parison hang times. The resin does not contain intentional slip or antiblock additives, and its natural color is intended for blender-fed pigment dosing or natural container production.

    Rheological and Mechanical Specification Profile

    The manufacturer’s published datasheet summarizes the physical properties used for incoming quality control and for finite-element simulation of blow-molded container performance. The following table consolidates the commonly referenced values measured under standard laboratory conditions. These values are typical and are not specification limits; lot-to-lot variation should be managed through the certificate of analysis and incoming inspection.

    Typical physical properties reported for Dow HDPE DMDJ-6200
    PropertyTest methodTypical value
    DensityASTM D1505-180.956 g/cm³
    Melt flow rate, 190 °C / 2.16 kgASTM D1238-200.60 g/10 min
    Tensile strength at yieldASTM D638-1427.6 MPa
    Elongation at breakASTM D638-14>800 %
    Flexural modulus, 1% secantASTM D790-171,140 MPa
    Hardness Shore DASTM D2240-1562
    Vicat softening temperatureASTM D1525-17e1126 °C
    Environmental stress crack resistance, 100% Igepal, Condition BASTM D1693-21>600 h

    The tensile yield value of 27.6 MPa is consistent with a 0.956 g/cm³ HDPE homopolymer and contributes to dimensional stability under axial compression in container top-load testing. A yield strength higher than that of LLDPE or LDPE does not indicate high-speed puncture toughness in all end-use conditions; the elongation at break above 800 % is sensitive to specimen thickness, draw rate, and molecular orientation. A flexural modulus of 1,140 MPa provides wall rigidity but also increases the blow-air pressure required to force the parison against the mold surface. Hardness of 62 Shore D serves as a rapid in-plant indicator of density-dependent surface durability, while the Vicat softening point of 126 °C is relevant only for short-term hot-fill exposure assessment, not for continuous-use temperature limits.

    Extrusion blow molding trials on shuttle machines with 65 mm barrier screws and 125 mm accumulator heads indicate that feed-zone temperatures below 170 °C generate excessive screw torque and poor melt-temperature uniformity, while die-head temperatures above 220 °C reduce parison melt strength and create yellowing in stagnant flow regions. A conventional barrel profile for continuous extrusion blow molding is 180 °C at the feed throat, 190–200 °C in the compression zone, 200–210 °C in the metering zone, and 195–210 °C at the die. Screw configurations with an L/D ratio of 24:1 to 30:1 and a compression ratio of 2.5:1 to 3.5:1, using barrier flights or a Maddock mixing section, improve melt homogeneity and reduce unmelted pellet carryover into the parison.

    What limits the processing window in continuous extrusion blow molding?

    Because DMDJ-6200 has a melt flow rate of 0.60 g/10 min, the melt-temperature window is narrower than that of high-flow injection-molding HDPE. At melt temperatures below 170 °C, the increased shear viscosity elevates extruder drive current and can produce parison surface roughness. At melt temperatures above 230 °C, chain scission becomes measurable as reduced melt strength and lower container top-load performance. Prolonged residence time above 240 °C should be avoided, especially in accumulator-head machines with stagnation zones, because degraded material can dislodge as gel-like defects in the bottle wall. Purging with a lower-flow polyethylene between color changes and shutdown under reduced barrel temperatures mitigate carbonized deposit formation. Mold cooling water at 10–25 °C is normally used; mold temperatures below 10 °C can cause surface porosity from condensation, and mold temperatures above 30 °C can extend cycle time without proportional improvement in wall crystallinity.

    When accumulator-head operations require controlled parison sag

    Accumulator-head blow molding of containers in the 10–30 L range requires a melt flow rate that is low enough to resist gravity-driven parison sag but high enough to fill the die bushing without excessive melt fracture. DMDJ-6200 at 0.60 g/10 min is positioned for parison lengths up to approximately 1.5 m; beyond that length, a fractional-melt HDPE may be required. Parison programming with a variable die gap is commonly run between 1.5 mm and 2.5 mm, depending on tool diameter and shot size. In field-level production, die gaps below 1.2 mm at high shear rates create shark-skin surface defects on the parison, while die gaps above 3.0 mm reduce programming authority and increase sidewall thickness variation. Blow-air pressure of 0.6–0.8 MPa and mold temperatures of 15–25 °C are typical for containers with a nominal wall thickness of 2.0 mm. Published data for this specific configuration is limited; these ranges are derived from general HDPE blow-molding practice rather than a single controlled study.

    Regulatory verification for DMDJ-6200 in food-contact, pharmaceutical, and consumer packaging is application-specific and must be confirmed against the current manufacturer’s regulatory status document. The testing framework commonly applied to this HDPE class includes the following standards.

    Regulatory and certification framework commonly applied to HDPE blow-molding resins
    Standard or regulationScopeTypical test target
    FDA 21 CFR 177.1520Olefin polymers for direct food contactExtractables and migration limits
    Commission Regulation (EU) No 10/2011Plastics in food contact materialsOverall migration < 10 mg/dm²
    USP <661.1> / USP <661.2>Plastic packaging systems for pharmaceutical productsPhysicochemical and biological reactivity
    REACH EC No 1907/2006Registration, evaluation, authorisation of chemical substancesSVHC content below regulatory threshold
    RoHS Directive 2011/65/EUElectrical and electronic equipment restrictionsLead, mercury, cadmium, hexavalent chromium, PBB, PBDE limits

    Operational boundary: if the resin has been stored at relative humidity above 60 %, drying for 2 h at 80 °C is required before melt processing to prevent surface defects. Continuous-use containment of strong oxidizing acids at temperatures above 60 °C or immersion in aromatic hydrocarbons is outside the intended application envelope for this HDPE grade. Compliance status must be confirmed with the manufacturer’s regulatory letter for the specific target market and additive formulation. A pigment masterbatch or processing aid selected by the converter can alter global migration values and should be evaluated separately under end-use conditions.

    The primary difference between DMDJ-6200 and injection-molding HDPE grades is flow. Injection-molding HDPE grades in the 20–60 g/10 min range fill thin-wall tools at high speed, whereas DMDJ-6200 at 0.60 g/10 min would generate high pressure drop and risk short shots in long flow-length molds. Fractional-melt HDPE grades below 0.30 g/10 min offer greater parison sag resistance for very large containers but can reduce output and die-gap control authority in smaller shuttle machines. Compared with film-grade HDPE, DMDJ-6200 is formulated for thick parison walls and high die swell, not for low-gauge film bubble stability. The grade is not a direct substitute for cross-linkable HDPE or for high-density copolymers with comonomer-modified ESCR intended for aggressive surfactant-containing contents. Its density of 0.956 g/cm³ provides higher stiffness than LLDPE and lower permeability than LDPE, but it has lower environmental stress-crack resistance than a medium-density polyethylene or a bimodal HDPE with comonomer content optimized for slow crack growth. Machine validation is required before replacing an existing blow-molding HDPE of similar melt flow rate, because die swell, parison programming, and pinch-off weld strength are tool-specific responses that cannot be fully predicted from melt flow rate alone.

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