Dow Hdpe Dgda6944

Dow HDPE DGDA6944

    • Product Name: Dow HDPE DGDA6944
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 634679
    Productname Dow HDPE DGDA6944
    Polymertype High Density Polyethylene (HDPE)
    Density 0.952 g/cm3
    Specificgravity 0.952
    Meltindex 190c 2 16kg 0.35 g/10 min
    Highloadmeltindex 190c 21 6kg 25 g/10 min
    Meltflowratio I21 I2 71
    Tensilestrengthatyield 25.5 MPa
    Tensilestrengthatbreak 33.1 MPa
    Elongationatbreak 600%
    Flexuralmodulus 1170 MPa
    Vicatsofteningpoint 126 C
    Meltingtemperature 131 C
    Brittlenesstemperature < -70 C
    Environmentalstresscrackresistance >1000 h (F50, 10% Igepal)
    Hardness Shored 65
    Thermalexpansioncoefficient 1.2E-4 /C
    Bulkdensity 0.58 g/cm3

    As an accredited Dow HDPE DGDA6944 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Dow HDPE DGDA6944 is supplied in 25 kg bags, palletized, or 1,000 kg bulk bags for industrial shipping.
    Container Loading (20′ FCL) 20′ FCL container loaded with palletized 25 kg bags of Dow HDPE DGDA6944, stretch-wrapped, labeled, and secured for ocean shipment.
    Shipping Dow HDPE DGDA6944 is a non-hazardous high-density polyethylene resin supplied as pellets. It is typically shipped in 25-kg bags, octabins, or bulk trucks/railcars. For transport, classify as non-dangerous goods; no UN number, hazard class, or special shipping papers required. Store dry, away from ignition sources.
    Storage Store Dow HDPE DGDA6944 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed to prevent moisture, dust, and contamination. Avoid prolonged outdoor exposure and stacking damage. Use appropriate handling to minimize static buildup. Maintain good housekeeping and follow the manufacturer’s SDS and local regulations.
    Shelf Life Store cool, dry, sealed, away from sunlight; Dow HDPE DGDA6944 has an indefinite shelf life under proper conditions.
    Application of Dow HDPE DGDA6944

    Dow HDPE DGDA6944 is processed on a single-layer high-stalk blown film line built around a 75 mm grooved-feed extruder with L/D 30:1 and a 100 mm spiral mandrel die. The pellet is fed at screw speed 90–140 rpm, with a barrel profile of 180–210 °C in the feed section, 215–230 °C in the compression zone, and 225–245 °C at the adapter and die. The resin is not pre-dried unless storage is exposed to relative humidity above 60%; surface moisture above 0.03 wt% at the hopper throat produces micro-voids and can be removed with a hopper dryer at 80 °C for 2 h. The bubble is suspended as a vertical stalk extending 8–12 die diameters above the air ring before radial inflation at a blow-up ratio of 3.2:1–4.0:1, converting to a layflat width of 500–650 mm at a gauge band of 9–15 µm. Gauge control relies on a capacitive thickness scanner with a standard deviation target below 0.4 µm; excursions above this value appear as hard gusset wrinkles in the finished vest sack and cause transfer jams on rotary bag machines running at speeds above 220 cycles/min. Die gap is held at 1.2–1.8 mm and the frost line is maintained 900–1200 mm above the air ring; a lower frost line collapses the stalk and a higher frost line lowers transverse direction Elmendorf tear measured under ASTM D1922-23. Formulation for this segment includes an antiblock masterbatch dosed at 0.08–0.12 wt% synthetic silica concentrate and an erucamide slip masterbatch at 0.03–0.06 wt% to keep the film-to-film coefficient of friction below 0.25 during printing and bag conversion. Slip masterbatch addition above 0.08 wt% is avoided because it shortens corona treatment decay to below 24 h and results in ink adhesion failure on flexographic prints. The converted vest sacks are sealed on a rotary sealing machine with jaw temperatures of 160–190 °C and dwell times of 0.3–0.6 s, producing retail carrier sacks with a bottom seal strength of at least 6 N/25 mm when tested by ASTM F88/F88M-23. Food-contact compliance is evaluated under 21 CFR 177.1520 for olefin polymers and Regulation (EU) No 10/2011, with migration testing performed according to EN 1186-1; the final package must not exceed the overall migration limit of 10 mg/dm² when the intended use is direct food contact. Heavy metal restrictions are screened against EU Directive 94/62/EC Article 11 and the CONEG model toxics limit of 100 ppm for the sum of lead, cadmium, mercury, and hexavalent chromium.

    What Limits a 30 µm Institutional Can Liner on a Low-Stalk Tower?

    Low-stalk bubble geometry changes the relationship between melt temperature and tear balance: the bubble is expanded within 200–400 mm of the air ring at a blow-up ratio of 3.0:1–4.5:1 and a melt temperature of 195–215 °C, which suppresses stalk stretching and yields a more balanced MD/TD tensile ratio than a high-stalk structure. A 90 mm grooved-feed extruder running at 110–150 rpm and a die gap of 1.0–1.6 mm produces 30 µm can liners with a thickness tolerance of ±2 µm; line output falls between 250 kg/h and 350 kg/h on a 200 mm die. This application does not require food-contact certification, but the finished sacks are commonly qualified under EN 13592 for household refuse sacks, which requires dimensional tolerance, tear resistance, and impact strength at specified fill weights. Dart impact is tested under ASTM D1709-22 Method B; tensile properties under ASTM D882-18; Elmendorf tear under ASTM D1922-23; and opacity under ASTM D1003-21. Closed-loop film scrap from the bag-making line is reintroduced at 15–30 wt% in the sheet-fed edge trim; above 30 wt% addition, transverse direction tear variability exceeds ±12% because the reprocessed fraction carries degraded low-molecular-weight tails that nucleate micro-cracks in the film. The liner is intended for wet and dry institutional waste and for use as a leakproof secondary bag inside rigid containers; it is not qualified for continuous contact with liquids above 40 °C, because creep rupture of the low-thickness sidewall accelerates under hydrostatic load at elevated temperature. Seal strength in the bottom gusset is verified on the converter line at a jaw temperature of 165–185 °C and a dwell of 0.4–0.8 s, with a minimum recorded value of 8 N/25 mm for the finished side seal.

    For temporary landfill cell covers and construction-site moisture barriers, the resin is processed on a large blown film tower fitted with a 250 mm spiral die, a blow-up ratio of 2.0:1–2.8:1, and a frost line height of 500–800 mm to produce layflat widths of 10–16 m at a thickness of 250–500 µm. Melt temperature is held at 200–225 °C, and the nip assembly uses a 70–90 °C water-cooled collapsing frame to prevent blocking of heavy-gauge film. The converter adds carbon black masterbatch at 2.0–3.0 wt% with a carbon black dispersion rating of at least 3 under ISO 11420 Method A to provide ultraviolet stabilization for exposed service; for translucent white covers, a hindered amine light stabilizer masterbatch is used at 0.10–0.30 wt%. Field seaming is performed with thermal wedge welders at 300–350 °C wedge temperature and 0.8–1.5 m/min travel speed; seam quality is evaluated by peel and shear tests under ASTM D6392-12 with a minimum peel strength of 5 N/mm for 250 µm film and 7 N/mm for 500 µm film. The temporary cover is not a primary containment geomembrane; if the specification requires long-term chemical containment, a dedicated HDPE geomembrane grade with a defined cell classification under ASTM D3350-21 and qualification under GRI-GM13 is substituted. For the temporary use case, the primary test suite comprises thickness per ASTM D5199-12, trapezoidal tear strength per ASTM D1004-13, and puncture resistance per ASTM D5748-19. The terminal product is a ballast-weighted panel used to suppress odor, reduce rainwater infiltration, and cover construction spoils; published data for long-term ultraviolet service of this specific configuration is limited, so service life beyond 12 months requires field inspection of surface cracking at monthly intervals.

    SegmentExtruder / dieDie gapMelt temperatureBlow-up ratioFilm gauge
    High-stalk retail vest sacks75 mm / 100 mm1.2–1.8 mm225–245 °C3.2:1–4.0:19–15 µm
    Low-stalk institutional can liners90 mm / 200 mm1.0–1.6 mm195–215 °C3.0:1–4.5:130 µm ±2 µm
    Temporary landfill covers250 mm spiral die1.8–2.5 mm200–225 °C2.0:1–2.8:1250–500 µm
    Multi-wall sack internal liner75 mm / 150 mm1.0–1.4 mm205–235 °C2.2:1–2.8:135–60 µm
    Three-layer coextruded core70 mm core / 150 mm die1.2–1.8 mm225–235 °C2.5:1–3.2:125–60 µm
    Silage cover film250 mm die1.8–2.5 mm200–225 °C2.0:1–2.8:1150–250 µm

    If a Multi-Wall Paper Sack Requires a 35 µm Internal Moisture Barrier

    Paper sack converters insert an HMW-HDPE blown film tube into three-ply or five-ply pasted valve sacks to protect cementitious powder, pet food meal, or hygroscopic chemicals from moisture ingress. The tube film runs at a blow-up ratio of 2.2:1–2.8:1, slit rewind width of 350–600 mm, die gap of 1.0–1.4 mm, and melt temperature of 205–235 °C. A slip masterbatch is dosed at 0.02–0.05 wt% to avoid blocking in the rewound roll, while antiblock is generally omitted because the film is sandwiched between paper plies. Corona treatment is specified at 38–42 dyn/cm; below 36 dyn/cm, water-based polyvinyl acetate adhesive does not wet the HDPE surface and ply separation occurs during sack filling. Heat-seal strength of the bottom gusset is measured per ASTM F88/F88M-23 with a minimum peel strength of 8 N/25 mm after a 0.5 s dwell at 170 °C. Moisture vapor transmission rate is tested under ASTM F1249-20 at 38 °C and 90% RH; the HDPE liner reduces moisture gain relative to unlined paper but it does not provide a gas barrier, as oxygen transmission remains above 1000 cm³/(m²·d·bar) at 23 °C and 0% RH. For food-contact applications, migration is assessed under 21 CFR 177.1520(c) and Regulation (EU) No 10/2011; for powdered chemicals, the assembled sack may require UN qualification under ADR/RID 6.1 for dangerous goods packaging, including stacking and leakproofness tests. The finished sack passes through a drop-impact sequence based on ISO 7965-2 or ISTA 1A; liner puncture during drop testing at 1.2 m is the dominant failure mode when the filled mass exceeds 25 kg.

    In a three-layer coextruded film for refrigerated produce or cereal liner packaging, the HMW-HDPE is placed in the core layer at 20–40 wt% of total film weight, with two LLDPE skin layers each contributing 30–40 wt%; the exact distribution is governed by the film modulus target and sealing initiation temperature. The core extruder uses a barrier screw and is operated at 210–235 °C, while the skin extruders run at 195–215 °C; feedblock and die temperatures are held at 225–235 °C. Gravimetric dosing tolerance of ±0.2 wt% on the HDPE core is maintained because excursions above 45 wt% core fraction create spiral die lines and weld-line roughness visible on the primary inspection winder. Blow-up ratio is set between 2.5:1 and 3.2:1, total film gauge at 25–60 µm, and line speed between 80 m/min and 150 m/min. The HDPE core increases secant modulus at 1% strain under ASTM D882-18 and reduces moisture vapor transmission compared with a 100% LLDPE control; published data for this specific sandwich configuration is limited, but converter measurements generally show a water vapor transmission rate reduction of 15–35% when the core fraction increases from 20 wt% to 40 wt% at constant gauge. The film is converted on vertical form-fill-seal machines with fin-seal jaw temperatures of 130–160 °C and back-seal dwell times of 0.2–0.4 s; the final pillow pouches are used for washed-cut produce, frozen cereal liners, and dry snack secondary packaging. Compliance for food contact is validated on the finished multilayer structure, because the HDPE core layer alone does not confer compliance; migration testing is performed under 21 CFR 177.1520 and Regulation (EU) No 10/2011, and the converter must consider the migration contributions of the skin resins and any tie-layer additives.

    Silage Cover Film Puncture and UV Stabilization Limits

    Silage clamp covers and temporary bunker covers are converted from HMW-HDPE blown film with a thickness of 150–250 µm, a blow-up ratio of 2.0:1–2.8:1, and a layflat width of 10–16 m on a 250 mm die. Outdoor service requires a UV-stabilizer masterbatch: hindered amine light stabilizer at 0.10–0.30 wt%, or carbon black masterbatch at 2.0–3.0 wt% for opaque black film. Carbon black dispersion must meet at least ISO 11420 Method A rating 3; poorer dispersion produces micro-defects that reduce slow puncture resistance and create localized crack initiation points under wind-induced flapping. Puncture resistance is measured by ASTM D5748-19 at 23 °C, Elmendorf tear by ASTM D1922-23, and low-temperature brittleness by ASTM D1790-21 because HDPE stiffens below −20 °C and may crack when repositioned on frozen forage. Field seaming uses 25 mm double-sided acrylic tape or thermal wedge welding; welded seams are evaluated by ASTM D6392-12 peel and shear methods with a minimum peel strength of 5 N/mm for 150 µm film. The cover is a physical rain shield, not an oxygen-barrier silage film; oxygen permeability remains above 300 cm³/(m²·d·bar) at 23 °C and 50% RH, so long-term fermented forage preservation requires a coextruded EVOH barrier layer or a separate oxygen-barrier film. The terminal product is weighted with sandbags or tire sidewalls and inspected for stress whitening at monthly intervals during the storage season.

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    Certification & Compliance
    More Introduction

    Dow HDPE DGDA-6944 is a high-density polyethylene extrusion resin supplied as natural pellets for outside-plant telecommunications cable jackets, conduit, and rigid profile applications. The grade occupies the high-modulus segment of HDPE, with a nominal melt index of 0.33 g/10 min at 190°C/2.16 kg under ASTM D1238 and a density near 0.955 g/cm³ under ASTM D1505, placing it below the flow-rheology range of general-purpose injection-molding HDPE and above the melt-flow range of high-molecular-weight film resins. Published mechanical values typically include tensile yield strength of approximately 27 MPa and tensile strength at break of approximately 29 MPa under ASTM D638, with flexural modulus near 1200 MPa under ASTM D790. Environmental stress-crack resistance measured by ASTM D1693 condition B in 10% Igepal at 50°C typically exceeds 1000 h F50, while oxidative induction time under ASTM D3895 at 200°C is typically above 40 min for compression-molded plaques. These values function as material-selection screening data and are not specification limits; release properties are governed by the current certificate of analysis and the manufacturer’s grade-specific technical data sheet.

    Grade classification and typical property envelope

    Within the polyethylene family, DGDA-6944 corresponds to the high-density class defined under ISO 1872-1 by density greater than 0.940 g/cm³ and an ethylene homopolymer backbone with limited short-chain branching. The relatively low melt index of 0.33 g/10 min produces higher shear viscosity than extrusion grades rated at 1.0 g/10 min and above, which restricts thin-wall flow length in injection molding but improves melt integrity during free-surface extrusion of cable jackets and tubes. Capillary rheometry on this class of HDPE at 190°C and 100 s⁻¹ generally indicates apparent viscosity in the 800–1000 Pa·s range, although published data for this specific configuration is limited and should be confirmed on the production lot. The density and molecular weight distribution contribute to a flexural modulus near 1200 MPa, permitting thinner sheath cross-sections under crushing loads than LLDPE jacketing compounds at density near 0.920 g/cm³.

    PropertyTest methodTypical value
    Melt indexASTM D1238, 190°C/2.16 kg0.33 g/10 min
    DensityASTM D15050.955 g/cm³
    Tensile strength at yieldASTM D63827 MPa
    Tensile strength at breakASTM D63829 MPa
    Elongation at breakASTM D638650%
    Flexural modulusASTM D7901200 MPa
    Shore D hardnessASTM D224066
    Vicat softening pointASTM D1525123°C
    Brittleness temperatureASTM D746< -76°C
    ESCR F50ASTM D1693, 10% Igepal, 50°C> 1000 h
    Oxidative induction timeASTM D3895, 200°C> 40 min

    On a single-screw extrusion line fitted with a 45 mm screw and 24:1 L/D barrel, DGDA-6944 is typically processed with feed zone settings of 160–170°C, compression zone settings of 190–200°C, and die zones at 205–215°C. The resin can be conveyed without pre-drying when ambient relative humidity remains below 60%; above that threshold, surface moisture can introduce surface gel defects in thin-wall jacket extrusion. Screw speed is set to maintain residence time below 8 min at melt temperatures below 220°C. At die land length-to-gap ratios between 10:1 and 15:1, back pressure typically stabilizes between 10 MPa and 20 MPa depending on breaker plate condition and screen-pack configuration. A 40/60/80 mesh screen pack is common in cable jacket production to remove carbonized particles, but pressure drop increases as screen area is reduced; published data for specific configurations is limited. Draw-down ratio in cable jacket applications is ordinarily held at 1.05:1 to 1.15:1 to limit molecular orientation and residual shrinkback after water-bath cooling.

    What separates DGDA-6944 from general-purpose HDPE extrusion resins?

    The primary difference is not density alone but the combination of moderate melt index, elevated environmental stress-crack resistance, and oxidation resistance. General-purpose HDPE pipe resins with melt index near 0.35 g/10 min may exhibit ESCR F50 below 100 h under the same ASTM D1693 condition B when formulated without the higher stabilizer loading and molecular architecture associated with telecommunications jacketing. DGDA-6944 is specified where the jacket must survive decades of soil contact, temperature cycling, and constant strain from tight coiling. Compared with LLDPE jacketing grades at density near 0.920 g/cm³, DGDA-6944 has flexural modulus approximately three times higher, allowing thinner sheath sections to resist crushing in duct applications. However, its low-temperature impact strength at -40°C is lower than LLDPE, and notch sensitivity increases with wall thickness. Compared with medium-density polyethylene jacketing at density near 0.935 g/cm³, the higher crystallinity of DGDA-6944 provides greater cut-through and heat deformation resistance but reduced conformability around irregular cable bundles.

    When thermal degradation limits the operating window at the die exit

    Thermal oxidation in DGDA-6944 is not detected solely as melt flow shift; it also appears as reduced extensional viscosity at the die, causing neck-in and loss of diameter control on thick jackets. Oxidative induction time under ASTM D3895 establishes the upper thermal exposure limit for the compounded stabilizer package, but the 40 min value at 200°C is a laboratory plaque measurement and should not be interpreted as a safe production residence time at that temperature. Shear heating in the metering section can create local temperature spikes above the barrel set point. For a 90 mm single-screw extruder with 30:1 L/D, barrel settings above 240°C are not recommended because chain scission accelerates and stabilizer consumption increases. Above this threshold, diameter variability and surface roughness often become process defects before bulk mechanical properties collapse. Published data for quantitative ESCR loss after repeated extrusion of this specific grade is limited, but the operational boundary is stated in manufacturer processing guides. Purge procedures at shutdown using a low-melt-index HDPE or inert gas atmosphere reduce carbonaceous deposits in the screw channels.

    Assessing environmental stress-crack resistance in buried service

    ESCR is not a single-valued material constant. The ASTM D1693 condition B test imposes a notch in a bent strip immersed in 10% Igepal at 50°C; F50 values above 1000 h indicate resistance to slow crack growth under fixed strain. For buried conduit, additional verification under ISO 22088-4 or notched pipe testing may be required because the tensile stress state in a constrained duct differs from the laboratory bent-strip configuration. In cable jacket extrusion, draw-down creates residual stress at the outer surface; annealing at 100°C for 1 h in a water bath reduces post-coiling shrinkback. In black jacketing compounds, carbon black masterbatch addition at 2.0–2.5 wt% with primary particle size below 60 nm improves ultraviolet resistance, but poor dispersion can act as an initiation site for slow crack growth under service loads. Extruders used for this grade should therefore be cleaned after carbon black color changes to avoid gel and unmelts in subsequent natural resin production.

    Applications outside cable jacketing include rigid agricultural conduit and equipment tubing where the same modulus and ESCR properties are utilized. Silo storage and pneumatic conveying of natural pellets should avoid contamination with polypropylene, because 5 wt% incidental PP can lower ESCR and create delamination in thick sections. The resin is not recommended for rotational molding or blown film below 0.5 mm thickness because the low melt index produces low bubble stability at commercial output rates. Food-contact suitability must be verified against the manufacturer’s current compliance documentation for the specific grade and packaging format, including 21 CFR 177.1520 status where applicable. In all cases, the processing window and final application performance should be revalidated on the production line using the certificate of analysis for the received lot.

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