Products

PetroChina Dushanzi HDPE DMDN-8008

    • Product Name: PetroChina Dushanzi HDPE DMDN-8008
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 211797
    Density 0.958 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 8.0 g/10 min
    Tensile Strength At Yield ≥26 MPa
    Elongation At Break ≥500%
    Flexural Modulus ≥1000 MPa
    Notched Izod Impact Strength ≥50 J/m
    Vicat Softening Point ≥125 °C
    Melting Point 130-135 °C
    Hardness Shore D 60-65
    Mold Shrinkage 1.5-3.0%
    Water Absorption <0.01%
    Dielectric Constant 2.3
    Volume Resistivity >10^16 Ω·cm
    Crystallinity 80-90%
    Molecular Weight Distribution Narrow
    Form Pellets
    Color Natural

    As an accredited PetroChina Dushanzi HDPE DMDN-8008 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PetroChina Dushanzi HDPE DMDN-8008: available in 25 kg woven bags, 40 bags per pallet (1000 kg), or 1000 kg jumbo bags.
    Container Loading (20′ FCL) PetroChina Dushanzi HDPE DMDN-8008 loaded in 20′ FCL containers: 25 kg bags, loose or palletized, approx. 20–25 MT net.
    Shipping PetroChina Dushanzi HDPE DMDN-8008 is a non-hazardous polyethylene resin, typically shipped as pellets in 25 kg bags, jumbo bags, or bulk. Transport in clean, dry, covered containers by truck, rail, or sea. Protect from moisture, heat, sunlight, and contamination. Standard shipping; no dangerous-goods handling required.
    Storage Store PetroChina Dushanzi HDPE DMDN-8008 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, and open flames. Keep bags or containers tightly closed to prevent moisture, dust, and contamination. Avoid contact with strong oxidizing agents. Stack pallets securely at moderate height. Use first-in, first-out stock rotation and follow local regulations and supplier recommendations.
    Shelf Life PetroChina Dushanzi HDPE DMDN-8008: store cool, dry, ventilated, away from sunlight; shelf life typically 24 months in unopened packaging.
    Application of PetroChina Dushanzi HDPE DMDN-8008

    Monolayer extrusion blow molding of DMDN-8008 for oxidizing household and industrial chemical cleaners begins with pellet-fed single-screw extruders of 60–90 mm diameter and 24:1–30:1 L/D, where melt temperature is held at 180–210 °C and die head temperature at 180–200 °C. The grade’s typical melt flow rate of 0.8 g/10 min under ISO 1133-1:2022 and density of 0.958 g/cm³ under ISO 1183-1:2019 place it within the blow molding window for shallow-thread, high-environmental-stress-crack-resistance containers. In this sector, virgin pellets are compounded with 2–4 wt% color or additive masterbatch and up to 30 wt% closed-loop edge trim regrind for non-food articles; higher regrind fractions reduce ESCR below acceptable limits for hypochlorite-containing formulations because oxidized segments and carbonyl groups accumulate through repeated heat histories. Finished containers for corrosive or oxidizing liquids are qualified under UN Model Regulations Chapter 6.1 and marked as UN 3H1/Y configurations when the closure and wall thickness combination passes drop, leakproofness, hydraulic pressure, and stacking tests at Packing Group II or III densities. Production is typically performed on accumulator-head shuttle machines with parison programming to maintain wall thickness from 0.6 mm to 2.2 mm, blow pressure of 0.6–0.8 MPa, and mold temperature of 10–30 °C; parison sag beyond 300 mm at 190 °C produces wall-thickness variation above 15% and weak pinch-off zones. Terminal products include 500 mL–25 L detergent, disinfectant, peroxide, and chlorinated cleaner bottles and jerry cans, with closure torque retention measured after 48 h storage at 40 °C.

    Does ESCR Alone Govern Solvent-Based Agrochemical Container Acceptance?

    It does not. Agrochemical containers produced from DMDN-8008 are not accepted solely by ESCR value. For cyclohexanone-, xylene-, or n-methyl-2-pyrrolidone-containing crop protection formulations, ESCR measured by ASTM D1693-B in 10% Igepal CO-630 at 50 °C is necessary but insufficient because weight loss through permeation, closure-seal softening, and label-panel delamination also determine field failure. Monolayer DMDN-8008 is therefore restricted to water-based suspension concentrates and soluble liquids; solvent-based products require in-line fluorination after molding or coextrusion with a polyamide barrier layer. The resin formulation in this sector uses 2–4 wt% UV stabilizer masterbatch, 0.5–1.0 wt% antistatic concentrate, and no more than 20 wt% production regrind; pigment loading above 2.5 wt% can reduce low-temperature drop impact at -18 °C. Extrusion blow molding parameters overlap with the industrial chemical sector, with melt temperature of 180–210 °C, die gap of 0.8–2.0 mm, and blow ratio between 1.8:1 and 2.5:1. Compliance is assessed under UN Model Regulations Chapter 6.1, ADR 6.1.3, and IMDG Code packaging provisions, with typical designations of UN 3H1/Y1.5/100 or UN 3H1/X1.5/100 depending on specific gravity and vapor pressure. Terminal articles are 100 mL–5 L agricultural chemical bottles and narrow-neck jerry cans, often tested for 28 days at 40 °C with the actual formulation to detect handle-area stress cracking and neck distortion.

    Oil-Based Food Contact Bottling and Organoleptic Transfer Boundaries

    Edible oil and condiment converters typically qualify DMDN-8008 for short-to-medium shelf-life bottles where oxygen ingress is controlled by bottle geometry, pigmentation, or secondary packaging rather than by the HDPE wall itself. In this end-use, only virgin resin is used, with food-grade color masterbatch at 2–4 wt%; regrind is excluded unless it comes from a closed-loop food-contact process and satisfies the relevant recycled-plastics framework. Extrusion blow molding is performed at 180–220 °C with clean, filtered blow air and polished molds; mold temperature is maintained at 12–22 °C to reduce contact transparency and improve surface stability. The resin’s migration behavior is judged under FDA 21 CFR 177.1520(c), EU No 10/2011, and GB 4806.6-2016, with additive positive-list verification under GB 9685-2016. Organoleptic transfer thresholds for oil simulant D2 under EU No 10/2011 must remain below the overall migration limit of 10 mg/dm² of contact area, although published data specific to DMDN-8008 in non-polyolefin food simulants is limited and end-use qualification is converter-specific.

    JurisdictionStandardTest MediumAcceptance Limit
    United StatesFDA 21 CFR 177.1520(c)Food oil, n-heptaneOlefin polymer compositional and density limits; no detectable migration exceedance
    European UnionEU No 10/2011Simulant D2, vegetable oilOverall migration ≤ 10 mg/dm²
    ChinaGB 4806.6-2016Food simulantsTotal migration ≤ 10 mg/dm²; positive-list additives only

    Terminal food-contact articles include 500 mL–5 L edible oil bottles, soy sauce bottles, and sauce dispensers. Long-chain fatty food contact is acceptable, but DMDN-8008 is not suitable for carbonated beverages, hot-filled products above 60 °C, or oxygen-sensitive oils requiring an oxygen transmission rate below 10 cm³/(m²·day·atm) without additional barrier modification.

    DMDN-8008 appears in high-gloss narrow-neck packaging for surfactant-based personal care formulations, where surface finish after extrusion blow molding and neck thread dimensional stability determine capping torque retention and e-commerce leakage resistance. In cosmetic bottle production, the resin is blended with pearlescent or color masterbatch at 1.5–3.5 wt%, and the melt is processed at 180–210 °C using polished aluminum molds held at 15–25 °C; blow pressure is set at 0.6–0.8 MPa and cycle time is adjusted to limit sink marks near the pinch-off. Packaging safety is assessed under REACH (EC) 1907/2006 and, where substance transfer to the cosmetic formula is possible, under EU 1223/2009 Article 17 as part of the cosmetic product safety assessment. The narrow processing window in this sector relates to neck calibration: insufficient calibration produces varying inner diameter and high cap leakage rates, while overcooling below 10 °C increases surface haze on high-gloss panels. Terminal products include 50–1000 mL shampoo, conditioner, body wash, and lotion bottles with smooth labeling panels and high-drop-impact resistance at refrigerator and bathroom storage temperatures.

    USP <661.2> Extractables and the Vial-to-Container Scaling Problem

    Pharmaceutical and nutraceutical container qualification uses USP <661.1> and USP <661.2> to evaluate plastics of construction, extractables, and finished packaging system suitability. DMDN-8008 can be considered for oral solid-dose HDPE tablet and capsule containers only when converters use 100% virgin resin, FDA-sanctioned color masterbatch at 1–2 wt%, and no regrind, because recycled content introduces unidentified extractables and batch-to-batch variability. Processing is typically continuous extrusion blow molding with melt temperature of 175–205 °C, particle-filtered blow air, and mold temperature of 10–25 °C; neck and thread dimensions are stabilized by in-mold calibration, and residual surface volatiles are reduced by post-mold air leaching. Compliance additionally references Ph.Eur. 3.1.3, FDA 21 CFR 177.1520, and ICH Q3D for elemental impurities where applicable. Published data for DMDN-8008 under USP <661.2> is limited; each finished package must be qualified with the actual drug product or nutritional formulation under 40 °C/75% RH stability protocols. Terminal products are 30–500 mL white or colored HDPE tablet and capsule bottles, usually paired with induction seals and child-resistant or continuous-thread closures separately qualified under USP <671>.

    If High-Speed 20 L Lubricant Pack Molding Runs Above 45 kg/h

    At line speeds exceeding 45 kg/h per single-screw extruder, automotive fluid packaging using DMDN-8008 shifts from simple blow molding to a heat-removal-limited process. For 1–20 L motor oil, automatic transmission fluid, coolant, and windshield washer containers, the grade is compounded with carbon black or UV masterbatch at 1.5–3.0 wt% and up to 30 wt% clean internal regrind; regrind above this level increases parison melt fracture and reduces drop-impact energy at -20 °C. Extrusion blow molding is performed on high-speed shuttle or single-station machines with screw diameter of 70–100 mm, L/D of 30:1, melt temperature of 180–210 °C, and mold temperature of 15–35 °C; post-cooling air or water jets are used to prevent neck and handle distortion. Compliance for engine oil and coolant containers relies on UN Model Regulations Chapter 6.1 when the finished pack is used for regulated liquids, with typical designations of UN 3H1/Y or UN 3H2/Y, depending on closure type and inner liner configuration. High-output lines must monitor screw-speed-induced shear heating above 220 °C, which can generate gel particles visible on the interior wall and reduce pinch-off burst strength below 0.1 MPa in pressure-holding tests. Terminal automotive aftermarket products include 1–20 L lubricant, coolant, and washer fluid containers; fuel-containing mixtures are excluded from monolayer DMDN-8008 unless fluorination or an approved barrier layer is used.

    Free Quote

    Competitive PetroChina Dushanzi HDPE DMDN-8008 prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618136850665

    Email: admin@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

    PetroChina Dushanzi HDPE DMDN-8008 is a bimodal high-density polyethylene supplied as a black, carbon-black-stabilized pellet for solid-wall pressure pipe extrusion. The product is designated by the producer as a PE100 high-density polyethylene under ISO 12162, with a minimum required strength of 10.0 MPa at 20°C for 50 years when evaluated according to ISO 9080. This pressure rating places DMDN-8008 in the class of pipe materials used for municipal water distribution, buried natural gas conveyance, and industrial fluid transfer where long-term hydrostatic integrity is the controlling requirement. The grade is differentiated from general-purpose HDPE injection and blow molding resins by its lower melt flow rate, bimodal molecular weight distribution, and carbon black stabilization. Typical published values include a melt flow rate of 0.80 g/10 min at 190°C under 5.00 kg load and a density of 0.949 g/cm³. The bimodal molecular architecture combines a high-molecular-weight fraction that contributes to slow crack growth resistance with a lower-molecular-weight fraction that reduces viscosity during extrusion. The pellet is black due to carbon black loading in the range of 2.0–2.5% by weight, which provides ultraviolet stabilization for outdoor storage and buried service after pipe manufacture. DMDN-8008 is not intended for injection molding, thermoforming, or film conversion; its high melt viscosity and high molecular weight produce excessive filling pressure in injection molds and poor draw-down in film lines. The product is typically converted on grooved-feed single-screw extruders with vacuum calibration, and finished pipe is joined by butt fusion or electrofusion under model-specific procedures.

    What Published Melt and Solid-State Properties Define DMDN-8008?

    The nominal properties in the table are used for initial material qualification, while finished pipe must be tested for hydrostatic design compliance according to the relevant pipe standard. The melt flow rate of 0.80 g/10 min is significantly lower than injection molding HDPE grades, which commonly range from 4.0 g/10 min to 20.0 g/10 min. The low flow rate increases melt pressure during pipe extrusion but provides the high molecular weight needed for slow crack growth resistance. The density of 0.949 g/cm³ is higher than HDPE film grades and contributes to pipe ring stiffness while maintaining resistance to rapid crack propagation in pressurized service.

    PropertyTest MethodTypical Value
    Melt flow rate, 190°C/5.00 kgISO 1133-10.80 g/10 min
    DensityISO 1183-10.949 g/cm³
    Tensile stress at yieldISO 527-223 MPa
    Elongation at breakISO 527-2>600%
    Flexural modulusISO 178850 MPa
    Carbon black contentISO 69642.0–2.5%
    Thermal oxidative induction timeISO 11357-6≥30 min at 200°C
    Notched pipe test for slow crack growthISO 13479≥500 h at 80°C

    During pipe extrusion, DMDN-8008 is typically processed on grooved-feed single-screw extruders with L/D ratios between 30:1 and 33:1, or on counter-rotating twin-screw extruders when highly filled or wide-diameter pipe formulations are used. Barrel temperature profiles are set from 180°C in the feed zone to 200°C in the metering zone, with adapter and die-head temperatures maintained between 195°C and 215°C. The measured melt temperature at the adapter should remain in the range of 190°C to 215°C. Sustained operation above 230°C can induce oxidative chain scission, increase gel counts, and reduce long-term hydrostatic strength even if short-term tensile properties appear unchanged. Vacuum calibration is standard for solid-wall pipe; melt pressure at the breaker plate is controlled between 15 MPa and 25 MPa depending on die diameter, wall thickness, and line speed. Screw speed and line speed must be adjusted on the specific extruder to maintain the required melt pressure without exceeding the thermal degradation limit. Pre-drying is not normally required when pellets are stored in sealed containers and protected from condensation. If pellets are exposed to relative humidity above 60% or exhibit surface frost, hopper drying at 80°C for 2 hours is recommended to prevent surface splay and microvoids in thick-walled pipe. The material should not be processed above 230°C, and residence time in the die should be minimized to prevent thermal oxidation. Regrind of clean pipe scrap may be incorporated at low addition rates, but each converter must validate hydrostatic strength because the addition of regrind can alter slow crack growth resistance. Injection molding of DMDN-8008 is not recommended due to high melt viscosity; thin-wall injection tooling can experience short shots, weld-line brittleness, and clamp force requirements beyond the range of machines designed for general-purpose HDPE.

    Slow Crack Growth Resistance and Hydrostatic Design Basis

    Resistance to slow crack growth is the principal differentiator in pressure pipe service. DMDN-8008 uses a bimodal molecular weight distribution and controlled comonomer placement to resist crack initiation and propagation under sustained hoop stress. In the notched pipe test according to ISO 13479, pipe specimens are notched axially and tested under internal pressure at 80°C in water; failure time indicates slow crack growth resistance. PE100 formulations typically exceed 500 h in this test, and converter validation should confirm grade-specific failure times under the target diameter and wall thickness. The hydrostatic design basis is established under ISO 9080 by testing pipe samples at multiple temperatures and hoop stresses; the data are extrapolated to 50 years using the standard’s regression procedures. ISO 12162 then assigns the material a PE100 designation if the lower confidence limit of long-term hydrostatic strength satisfies 10.0 MPa at 20°C. This value is 25% higher than the 8.0 MPa minimum required strength for PE80 materials. As a result, a PE100 pipe can be designed with a thinner wall than a PE80 pipe for the same pressure rating, or it can carry a higher pressure at the same wall thickness, subject to the limits of ISO 4427 for water and ISO 4437 for gas. The carbon black content of 2.0–2.5% by weight also provides resistance to ultraviolet embrittlement, allowing outdoor storage and direct burial without additional UV stabilizer. However, carbon black cannot protect against oxidative attack from strong oxidizers, and chemical compatibility must be evaluated for each conveyed medium. Rapid crack propagation resistance is evaluated using the full-scale critical pressure test ISO 13477 at low temperature. PE100 compounds are designed to arrest rapid cracks; the material’s density and molecular weight are balanced to avoid brittle crack propagation at operating pressures.

    When DMDN-8008 Is Benchmarked Against Unimodal HDPE Grades

    In pressure pipe service, the distinction between DMDN-8008 and a general-purpose unimodal HDPE is defined by molecular architecture, melt flow, and long-term pressure rating. A unimodal injection HDPE with a comparable density of 0.949 g/cm³ but a melt flow rate of 4.0 g/10 min to 20.0 g/10 min can be molded into thin-wall articles, but it does not possess the high-molecular-weight fraction needed to meet PE100 hydrostatic requirements. The table below summarizes the key differences.

    CharacteristicDMDN-8008General-Purpose Unimodal HDPE
    Melt flow rate, 190°C/5.00 kg0.80 g/10 min4.0–20.0 g/10 min
    Molecular architectureBimodalUnimodal
    Hydrostatic design classificationPE100, 10.0 MPaNot rated for pressure pipe
    Primary processing routePipe extrusionInjection molding, thin-wall parts
    Typical failure concern in serviceSlow crack growth, oxidative degradationImpact, dimensional instability

    Compared with black PE80 pipe compounds, DMDN-8008 permits a higher allowable hydrostatic design stress but requires tighter extrusion temperature control. Compared with HDPE blow molding grades, DMDN-8008 has higher melt strength and a narrower processing window for parison formation; the same melt strength reduces sag in large-diameter pipe extrusion. In buried gas distribution, pipe produced from DMDN-8008 is joined by butt fusion under ISO 21307 or by electrofusion under ISO 12176; fusion parameters must be revalidated when changing from a unimodal pipe resin because the bimodal distribution changes melt flow and bead formation behavior.

    In buried potable water networks, pipe manufactured from DMDN-8008 is installed as solid-wall PE100 pipe with diameters commonly ranging from 16 mm to 1200 mm, depending on the converter’s line capability and wall-thickness control system. Finished water pipe is specified under ISO 4427 and, in the Chinese market, GB/T 13663, while natural gas distribution pipe is specified under ISO 4437 and GB 15558.1. For potable water service, the pipe must also meet national hygiene requirements for contact with drinking water; the resin and pipe compound must be evaluated for migration and organoleptic properties according to the applicable national or regional certification scheme. In gas service, the same PE100 hydrostatic performance is combined with rapid crack propagation resistance evaluated under ISO 13477. Industrial applications include pressure transfer of slurries, dewatering lines, cooling water circuits, and chemical solutions where compatibility data indicate no reduction in long-term strength. DMDN-8008 is not suitable for continuous exposure to strong oxidizing acids, aromatic hydrocarbons, or chlorinated solvents without permeation and environmental stress cracking review. For chlorine-containing potable water systems, long-term performance should be assessed under the relevant chlorine resistance test method adopted by the certifying body, as chlorine accelerates surface embrittlement in polyethylene. Outdoor storage of black DMDN-8008 pipe is generally acceptable because the carbon black loading of 2.0–2.5% by weight limits ultraviolet degradation; however, prolonged storage in high-temperature conditions can accelerate antioxidant depletion. Before pressure testing, all butt-fusion and electrofusion joints must be cooled under manufacturer-specified pressure and alignment parameters to prevent residual stress concentrations in the pipe wall.

    Top