| HS Code | 717984 |
| Density | 0.948 g/cm³ |
| Melt Index 190 C 2 16 Kg | 0.08 g/10 min |
| Tensile Strength At Yield | 23 MPa |
| Tensile Strength At Break | 32 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1.00 GPa |
| Hardness Shore D | 60 |
| Vicat Softening Point | 124 °C |
| Brittleness Temperature | -70 °C |
| Environmental Stress Crack Resistance | >5000 h |
| Thermal Conductivity | 0.400 W/m·K |
| Specific Heat Capacity | 1.90 J/g·°C |
| Water Absorption | 0.010% |
| Dielectric Constant | 2.3 |
| Volume Resistivity | 1.00e+16 ohm·cm |
As an accredited Dow HDPE DGDC-2480 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dow HDPE DGDC-2480 is supplied in 25 kg polyethylene-lined paper bags, palletized, or 1,000 kg bulk sacks for industrial use. |
| Container Loading (20′ FCL) | Dow HDPE DGDC-2480 resin loaded in 20-foot FCL container; palletized 25 kg bags, securely stowed and lashed for ocean shipment. |
| Shipping | Dow HDPE DGDC-2480 is a non-hazardous polyethylene resin. It is typically shipped in 25-kg bags, 1,000-kg jumbo bags, or bulk trucks/railcars. No DOT/IMDG/IATA dangerous-goods classification or special placards are required. Keep containers sealed, dry, and away from excessive heat and contamination; follow the SDS and local rules. |
| Storage | Store Dow HDPE DGDC-2480 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original containers or bags closed, clean, and clearly labeled. Protect from moisture, dust, and prolonged UV exposure. Use proper stacking limits to prevent deformation or rupture. Follow local regulations and Dow’s SDS for safe handling and storage. |
| Shelf Life | Dow HDPE DGDC-2480 has a shelf life of 12 months when stored in its original packaging under cool, dry conditions. |
Vehicle fuel tanks manufactured from DGDC-2480 are processed on accumulator-head extrusion blow molding lines with single-screw extruders in the 80–120 mm diameter range, run at 24:1–32:1 L/D with barrier screws and grooved feed sections. The barrel profile is typically set from 180°C at the feed throat to 210°C at the die head, while the mold shell is held between 20°C and 40°C to balance quench rate and surface gloss. Under these conditions the resin’s nominal high-load melt index of 7.0 g/10 min at 190°C/21.6 kg per ASTM D1238 and density of 0.945 g/cm³ per ASTM D1505 allow parison hang times sufficient for 60–90 L tank bodies without the necking collapse observed with lower-molecular-weight HDPE grades. The final tank wall is typically 4–8 mm, with polyethylene pinch-off welds consolidated at 0.7–1.0 MPa blow gas pressure and trimmed in-mold to avoid weld-line stress concentrations. For monolayer tank construction, no mineral filler is used; for six-layer coextruded fuel tanks, DGDC-2480 forms the inner and outer layers while an EVOH barrier layer is embedded at 2–3 wt% of the total structure with tie resins. Monolayer tanks are post-fluorinated, and inline fluorination or post-mold surface treatment at 0.5–1.5 atomic% fluorine within the top 5–10 µm reduces hydrocarbon permeation by roughly 90–99% relative to untreated HDPE. Tank assemblies are qualified under UN ECE R34 and FMVSS 301, with permeation testing per SAE J2659 at 40°C. Published data for this specific monolayer and fluorination configuration is limited, so barrier values must be confirmed on the production tank geometry rather than extruded plaques.
UN-rated industrial containers blow molded from DGDC-2480 are produced as tight-head 30 L, 60 L, and 220 L drums on high-force accumulator machines. The accumulator head shot capacity is matched to the part weight, typically 2–6 kg for 30–60 L containers and 8–12 kg for 220 L drums. Melt temperature is kept below 210°C to limit molecular weight degradation, while the mold temperature is held at 10–25°C to shorten demold time while maintaining environmental stress crack resistance. The base resin is let down with 0.5–1.5 wt% of carbon black or UV masterbatch only when outdoor storage is specified; for clean chemical service, natural resin is used to avoid additive contamination. Regrind from the same production lot may be incorporated at 10–25 wt%, but only after a lot-specific extractables check when the packaging is intended for food contact or high-purity solvents. The dominant field failure mode is environmental stress cracking at sharp radiused corners and pinch-off flash when the container experiences stacked creep at 40°C warehouse conditions. DGDC-2480’s ESCR under ASTM D1693-15 Condition A is typically reported as an F50 value greater than 600 h, which supports selection for long-term storage of nonionic surfactants, dilute acid, and aliphatic hydrocarbons. Compliance is demonstrated under ADR/RID Chapter 6.1, IMDG Code 6.1.5, and 49 CFR 178.504 for UN 3H1 packagings. The drop test is run at 1.2 m for packing group II and 1.8 m for packing group I after conditioning at −18°C; the hydrostatic proof test pressure is set according to the specific packing group and vapor pressure requirements of ADR 6.1.5.6. These containers are used for cleaning agents, liquid fertilizers, water treatment chemicals, and polar solvents in the 5–220 L range.
| Downstream application | Governing standard or code | Critical test condition | Relevant DGDC-2480 property |
|---|---|---|---|
| Automotive fuel tank | UN ECE R34, FMVSS 301, SAE J2659 | 40°C permeation, low-temperature impact | HLMI 7.0 g/10 min, parison integrity |
| UN 3H1 chemical drum | ADR/RID 6.1, IMDG Code 6.1.5, 49 CFR 178.504 | −18°C drop, stack test | ESCR F50 > 600 h |
| Food-contact sheet | FDA 21 CFR 177.1520(c) 3.2a, EU 10/2011 | Overall migration | Virgin resin only |
| Outdoor welded containment | DVS 2205-1, REACH, RoHS | Weld factor tensile test | Brittleness temperature < −75°C |
Sheet extrusion of DGDC-2480 is run on 90–150 mm single-screw extruders with 30:1–36:1 L/D barrier screws and static mixers upstream of a flat die. Melt temperature at the die exit is controlled between 200°C and 215°C. The three-roll polishing stack is set to 70–95°C on the top roll and 80–100°C on the middle roll; lower roll temperatures improve surface gloss but reduce sheet impact strength if the quench is too rapid. Thickness uniformity is governed mainly by die bolt adjustment and roll gap rather than polymer flow, but the high molecular weight of DGDC-2480 produces measurable die swell and edge bead that must be trimmed. Sheet thickness for thermoforming ranges from 1.5 mm to 8.0 mm. The sheet is suitable for plug-assisted thermoforming at surface temperatures of 150–170°C, with cavity pressure 0.5–0.8 MPa and aluminum tooling maintained at 50–70°C. Draw ratios above 2:1 in deep geometries produce non-uniform wall sections because the material does not flow readily in the solid state; this is not a limitation of the resin but a characteristic of HMW-HDPE. The resulting liners and trays are used as automotive wheel-well liners, battery acid containment trays, material-handling dunnage, and corrosion-resistant sump liners. Low-temperature ductility is assessed by ASTM D638 elongation at break above 600% and by notched Izod per ASTM D256 at −40°C. For general industrial service, compliance is limited to REACH and RoHS; food contact requires virgin-sheet confirmation under FDA 21 CFR 177.1520(c) 3.2a and EU 10/2011 migration testing, and the use of regrind is disallowed unless the specific lot is approved by the converter’s HACCP plan.
Stacked agrochemical packagings blown from DGDC-2480 on shuttle extrusion blow molders are produced with 60–80 mm extruders, 24:1 barrier screws, and 1+1 to 4+4 cavity configurations depending on container volume. Shot sizes for 10–25 L jerry cans are typically 1.2–2.8 kg. The melt is kept at 185–205°C, and the lower processing window boundary is set by the frost-line behavior of the parison rather than screw torque. Outdoor-stable formulations incorporate 1.5–2.5 wt% of a hindered-amine-stabilized carbon black masterbatch; the carbon black loading in the finished wall is maintained at 2–2.5 wt% to achieve the UV resistance required for multi-season agricultural use. Handle pinch-off regions and molded thread chimes are the critical stress concentration points. The wall thickness in those zones is typically increased 10–20% above the nominal 1.2–1.8 mm body wall by adjusting parison programming. For pesticide and liquid fertilizer service, the resin grade must show ESCR F50 above 600 h under ASTM D1693; when non-ionic surfactant exposure is expected, testing in the end-use formulation is required because Igepal-based screening does not fully reproduce field cracking. Containers shipped with hazardous liquids follow UN 3H1 testing under ADR/RID and 49 CFR 178.504; the closure-to-neck thread engagement is qualified by leakproof testing after the relevant drop condition. The finished parts carry in-mold or post-mold UN marking and packing group identification.
Windshield washer reservoirs, coolant overflow bottles, and HVAC fluid bottles are extrusion blow molded from DGDC-2480 using continuous parison shuttles with 50–70 mm extruders. The grade’s high melt strength permits the long, flattened parison shapes required for 1–5 L automotive reservoirs with convoluted neck offsets. Barrel temperatures are set between 190°C and 210°C; mold temperatures of 15–30°C are preferred for acceptable cycle times. The formulations are simpler than fuel tanks: neat natural resin or 1–2 wt% color masterbatch, with 10–20 wt% clean plant regrind allowed when the application is not safety-critical. The resin does not require predrying, but when warehouse humidity exceeds 60% RH and regrind is used, surface moisture can generate splay at the die exit; a 2–4 h hopper dryer at 70–80°C eliminates the defect. Long-term service conditions include −30°C winter cycling and sustained exposure to 50% ethylene glycol/water at 90°C under hood, which makes environmental stress cracking resistance critical. The reservoir must retain low-temperature impact after 500 h of hot coolant aging; the suitability of DGDC-2480 for this specific fluid is supported by its ESCR performance but must be confirmed by in-service validation because published data for this specific configuration is limited. These components are not covered by ECE R34 unless they are part of a fuel system, but automotive supply contracts commonly require material compliance with IMDS and REACH.
Sheet produced from DGDC-2480 at 3–8 mm thickness is cut and joined by hot-gas welding at 200–230°C with HDPE welding rod of the same resin family; extrusion welding with 3–4 mm rod and a 180–220°C melt zone produces homogeneous joints. Weld factor, defined as the tensile strength of the welded joint over the parent sheet, is typically quoted as 0.7–0.9 for correctly preheated HDPE, and the stress-cracking resistance of the heat-affected zone is the limiting property rather than short-term tensile strength. The base resin’s low-temperature ductility is relevant for outdoor service in northern climates where overnight temperatures below −30°C occur; notched Izod per ASTM D256 at −40°C and brittleness temperature per ASTM D746 below −75°C are the control points. In dilute sulfuric acid and sodium hydroxide containment, DGDC-2480 sheet demonstrates the HDPE-typical resistance profile: continuous service is limited to pH 1–14 at temperatures below 60°C, while strong oxidizers and aromatic solvents are excluded. The final fabrication is not regulated as a pressure vessel; structural design follows DVS 2205-1 for thermoplastic storage tank calculation. Published data for this specific resin in welded fabrication is limited, so weld qualification on production sheet is advised before installation.
Competitive Dow HDPE DGDC-2480 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
Flexible payment, competitive price, premium service - Inquire now!
Dow HDPE DGDC-2480 is described in manufacturer literature as a bimodal high-density polyethylene extrusion resin intended primarily for pressure-pipe applications. The grade is positioned within the PE100 designation because long-term hydrostatic strength data, evaluated in conformance with ISO 9080:2012 and classified under ISO 12162, correspond to a minimum required strength of 10 MPa at 20 °C. The defining structural feature is the bimodal molecular-weight distribution: a high-molecular-weight fraction supplies tie-molecule density and slow crack growth resistance, while a lower-molecular-weight fraction reduces melt viscosity and improves shear thinning during high-output pipe extrusion. Published product information identifies the resin as suitable for water and industrial pressure service; suitability for gaseous fuel piping must be confirmed against ISO 4437-1 and the specific black-compound dispersion requirements of the pipe standard.
Under ISO 12162, polyethylene pressure-pipe materials are ranked by the minimum required strength extrapolated to 50 years at 20 °C: PE63 grades support 6.3 MPa, PE80 grades support 8.0 MPa, and PE100 grades support 10 MPa. The change in classification from PE80 to PE100 therefore increases the allowable hydrostatic design stress by 25% when the same design coefficient is applied. A bimodal PE100 resin such as DGDC-2480 achieves this through a dual-reactor molecular architecture rather than through a simple melt-index reduction. Unimodal HDPE grades can attain high molecular weight only by raising the overall viscosity, which limits extrudability and can create excessive shear heating at high screw speed. In a bimodal system, the high-molecular-weight fraction carries most of the slow crack growth resistance, while the low-molecular-weight fraction acts as an internal processing aid. The practical difference is that the pipe producer can maintain stable melt pressure and acceptable motor load at output rates that would be problematic for unimodal HDPE of comparable density.
For extrusion-grade control, the melt mass-flow rate is determined at 190 °C under a 5.0 kg load using ISO 1133-1:2022. PE100 pipe extrusion grades conventionally fall within a meltflow window of 0.20–0.35 g/10 min, though the lot-specific certificate of analysis must be consulted for acceptance. Density by ISO 1183-1:2019 is typically within the 0.940–0.960 g/cm³ envelope used for high-density polyethylene pipe compounds. Published data for this specific configuration is limited, but thermal analysis by ISO 11357-1 places the crystalline melting peak for ethylene-rich HDPE in the 128–135 °C range and the crystallization peak near 116–120 °C. These thermal boundaries are operationally significant: the barrel profile must deliver enough thermal work to complete plasticization without allowing the melt to remain above the oxidative stability limit for excessive residence time.
For buried and trenchless pressure pipes, slow crack growth is the dominant long-term failure mode at service pressures below the burst limit. The high-molecular-weight fraction of the bimodal distribution increases the number of tie molecules connecting crystalline lamellae, which delays crack advance through the amorphous phase. Comparative slow crack growth evaluation is performed with the notched pipe test ISO 13479, in which a circumferential notch is machined into the pipe wall and hydrostatic stress is applied at 80 °C. PE100-grade compounds are generally expected to exceed 500 h at 4.0 MPa under notched conditions, although the pass/fail threshold depends on the product standard and may reach 1,000 h for higher-class PE100-RC listings. Rapid crack propagation is separately characterized by ISO 13477, which measures crack arrest after impact on a pressurized pipe. PE100 pipe resins typically show arrest below -10 °C; the exact critical temperature is influenced by pipe diameter, wall thickness, and extrusion-induced orientation. The combination of slow crack growth resistance and rapid crack propagation arrest is the principal technical justification for selecting a DGDC-2480-class material over standard high-density blow-molding or injection-molding grades in large-diameter water transmission and industrial piping.
Capillary rheometry under ISO 11443 shows that bimodal PE100 pipe grades display more pronounced shear thinning than unimodal high-density polyethylene of equal melt mass-flow rate. At extrusion shear rates between 10 s-1 and 100 s-1, the bimodal resin reduces melt viscosity rapidly, which translates into lower head pressure at high screw speed and reduced risk of melt fracture at the die lip. The product is therefore less sensitive to throughput-induced pressure spikes than a conventional high-density polyethylene with similar density but narrower molecular-weight distribution. This does not eliminate the need for correct screen-pack selection, melt-pump control, and die-land temperature uniformity. It does, however, provide a wider stable processing window for grooved-feed single-screw extruders with L/D ratios of 30:1 to 36:1.
Acoustic emissions and melt-pressure monitoring on production-scale pipe extrusion lines indicate that feed-zone instabilities can arise when screw speed is increased before the feed-zone barrel temperature reaches its steady-state plateau. For PE100-type grades, the feed zone is normally maintained at 180–200 °C, the compression zone at 190–210 °C, the metering zone at 200–220 °C, and the die head at 210–230 °C. Melt temperature measured at the die should remain below 240 °C. Prolonged residence above 250 °C accelerates thermo-oxidative chain scission, increases gel formation on the screen pack, and can produce surface roughness or gloss variation. When regrind is introduced above 20 wt%, hopper drying at 70–80 °C for 2–4 h reduces moisture-driven melt-pressure fluctuation. Published data for this specific configuration is limited, but these processing boundaries are consistent with general PE100 pipe extrusion technical bulletins and machinery operating specifications for grooved-feed extruders.
| Standard / test method | Property or role | Class-typical PE100 window |
|---|---|---|
| ISO 9080:2012 | Long-term hydrostatic strength extrapolation | 50-year hoop strength basis; MRS 10 MPa |
| ISO 12162 | Classification and designation of pressure-pipe thermoplastics | PE100 designation; design coefficient per product standard |
| ISO 1133-1:2022 | Melt mass-flow rate | 0.20–0.35 g/10 min at 190 °C/5.0 kg |
| ISO 1183-1:2019 | Density | 0.940–0.960 g/cm³ |
| ISO 13479 | Notched pipe slow crack growth | >500 h at 80 °C and 4.0 MPa; product-specific |
| ISO 13477 | Rapid crack propagation full-scale test | Arrest below -10 °C typical |
| ISO 11357-6 | Oxidative induction time | >20 min at 200 °C for stabilized pipe compound |
Values in the third column are class-typical PE100 extrusion-grade windows, not lot-specific certificate data. Product-specific certificates of analysis must be consulted for acceptance. Omission of an edition year for some pipe standards reflects the need to use the version invoked by the relevant product specification.
| Class | Minimum required strength at 20 °C | Design implication |
|---|---|---|
| PE63 | 6.3 MPa | Lower allowable pressure; thicker wall at equal design pressure |
| PE80 | 8.0 MPa | Intermediate pressure ratings; common in older distribution lines |
| PE100 | 10 MPa | Higher allowable hoop stress; thinner wall or higher operating pressure |
Potable-water pipe compounds based on this resin are applicable under ISO 4427-1, with the hydrostatic design stress determined by the minimum required strength divided by the overall service design coefficient. For natural-gas distribution, ISO 4437-1 normally applies; the final pipe compound must contain carbon black at 2.0–2.5 wt% with dispersion rating meeting ISO 18553. In industrial service, ISO 15494 may govern system design. The resin’s oxidation-inhibitor package must be compatible with the disinfectant regime in potable-water service. Incompatible additive combinations can reduce oxidative induction time below the end-use expectation and shorten service life at elevated pipe-wall stress.
Chemical-resistance classification under ISO/TR 10358 places high-density polyethylene in a limited-resistance category for strong oxidizing agents such as concentrated nitric acid and for certain aromatic and chlorinated solvents when surface stress exceeds the environmental stress-cracking threshold. Allowable service stress decreases as the operating temperature approaches 60 °C, and continuous exposure above 80 °C is outside the normal long-term pressure-service boundary for PE100 pipe materials. Outdoor storage of natural resin before compounding should be minimized because unstabilized natural pellet is not a substitute for carbon-black-protected pipe compound. Black pipe conforming to ISO 4427 and ISO 4437 includes carbon black specifically to provide ultraviolet protection for long-term above-ground or storage exposure.
Quality control for DGDC-2480 pipe production should include lot-to-lot melt mass-flow rate verification, density measurement, and thermal oxidative stability screening. On the extrusion line, continuous monitoring of melt temperature, head pressure, screw load, and ultrasonic wall-thickness profile is used to detect shifts in regrind ratio or feed-bridge plugging. A rising head pressure at constant screw speed without a corresponding change in melt temperature often indicates gel accumulation on the screen pack or unmelted material reaching the filter. In such cases, melt filtration is inspected, the screen pack is replaced, and the barrel profile is checked before the line is returned to the qualified production window. These operational limitations are inherent to high-molecular-weight HDPE pipe extrusion and are not unique to DGDC-2480, but they are more pronounced than with lower-viscosity general-purpose high-density grades.