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Shanxi PCEC HDPE DMDA8008

    • Product Name: Shanxi PCEC HDPE DMDA8008
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 704225
    Materialtype High Density Polyethylene
    Grade DMDA8008
    Density 0.954-0.955 g/cm³
    Meltflowrate 8.0 g/10 min at 190°C/2.16 kg
    Tensilestrengthatyield ≥25 MPa
    Elongationatbreak ≥500%
    Flexuralmodulus ≥1000 MPa
    Notchedizodimpactstrength ≥50 J/m
    Vicatsofteningtemperature ≥125 °C
    Heatdeflectiontemperature 70-75 °C
    Shoredhardness 65-66
    Moldshrinkage 1.5-3.0%
    Waterabsorption <0.01%
    Dielectricstrength ≥20 kV/mm
    Volumeresistivity ≥1×10^16 Ω·cm
    Thermalconductivity 0.40-0.45 W/m·K
    Specificheat 1.8-1.9 kJ/kg·K

    As an accredited Shanxi PCEC HDPE DMDA8008 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Shanxi PCEC HDPE DMDA8008 is packed in 25 kg PP woven bags, palletized and stretch-wrapped for secure industrial transport.
    Container Loading (20′ FCL) 20′ FCL container loaded with Shanxi PCEC HDPE DMDA8008 in 25 kg bags, palletized, shrink-wrapped, and secured for ocean transport.
    Shipping Shanxi PCEC HDPE DMDA8008 is shipped as non-hazardous thermoplastic resin pellets in 25 kg PP bags, jumbo bags, or bulk containers. Store in a dry, cool, ventilated area away from direct sunlight, heat, and ignition sources. Handle with standard PPE; avoid dust generation and environmental release.
    Storage Store Shanxi PCEC HDPE DMDA8008 in a cool, dry, well-ventilated warehouse, away from direct sunlight, rain, moisture, heat, and ignition sources. Keep original bags sealed, palletized, off the floor, and away from strong oxidizers, acids, and solvents. Avoid package damage, contamination, and excessive stacking. Maintain clean handling areas and follow local safety regulations.
    Shelf Life For Shanxi PCEC HDPE DMDA8008, store cool, dry, ventilated, away from sunlight; typical shelf life is 24 months in unopened packaging.
    Application of Shanxi PCEC HDPE DMDA8008

    Shanxi PCEC HDPE DMDA8008 is deployed in thin-wall injection-moulded food packaging where wall stock lies between 0.5 mm and 0.9 mm, specifically dairy tubs, delicatessen cups, and dry-food portion cups. The grade is controlled under ASTM D1238 at 190°C/2.16 kg as a high-flow HDPE, and density is controlled under ASTM D792 in the 0.963–0.965 g/cm³ range. In high-cavitation tools with 16 to 32 cooling-assisted cavities, the narrow-molecular-weight distribution reduces post-demoulding warpage, but the same narrowness compresses the hold-pressure window because the melt leaves the flow path more quickly than a broad-MWD HDPE. Processors running accumulator-assisted hydraulic machines with clamp forces of 1,800–3,500 kN and injection screw L/D ratios of 20:1–24:1 typically set melt temperatures between 225°C and 245°C, while mould coolant inlet temperature is held at 10–15°C with high-flow channels of 8–10 mm diameter placed 6–8 mm behind the cavity steel. Injection velocity is commonly maintained at 250–450 mm/s to fill thin sections before freeze-off; hold pressure is set between 35 MPa and 55 MPa with a pressure-stage time of 0.5–0.8 s for a 0.6 mm wall. Gate geometry is critical: direct pin gates of 0.8–1.2 mm or hot-runner valve gates with 1.0–1.5 mm nozzle orifices are used to prevent jetting and flow marks. With a high-flow grade in a 24-cavity dairy tub tool, total cycle times are commonly reported in the 4.5–7.0 s range on a press with an empty-dry-cycle time near 6 s. The finished containers are used for cold-fill dairy, deli salads, and dry food portions. Food-contact compliance requires verification under United States 21 CFR 177.1520(c) 3.2a for olefin polymers, European Union Commission Regulation (EU) No 10/2011 with overall migration below 10 mg/dm² in aqueous and fatty simulants according to EN 1186-1, and China GB 4806.7 for polyolefin food-contact materials where domestic production is placed on the market. A pigment masterbatch is limited to 2.5 wt% of an FDA-compliant white TiO₂ or black carbon-black system because higher loadings have been associated with gate blush and marginal melt-flow instability in thin-wall sections. Pre-drying is not mandatory at pellet surface moisture below 0.08%, but condensation on cold pellets in humid coastal warehouses should be managed by a hopper-air unit delivering 1 h at 70°C before processing.

    Regulatory marketControl frameworkNumerical limit or test condition
    United StatesFDA 21 CFR 177.1520(c) 3.2aOlefin polymer extraction, condition-of-use dependent
    European UnionCommission Regulation (EU) No 10/2011; EN 1186-1Overall migration < 10 mg/dm²
    ChinaGB 4806.7; GB 31604.1Overall migration ≤ 10 mg/dm²

    What changes in closure thread conformity when DMDA8008 replaces lower-flow HDPE at 64 cavities?

    Cap stock converters running high-cavitation hot-runner tools observe a modified filling balance when DMDA8008 is introduced on an existing 32- or 64-cavity mould originally qualified for a 4 g/10 min HDPE. Because the melt index measured under ASTM D1238 at 190°C/2.16 kg is positioned near 8 g/10 min, the pressure drop from machine nozzle to cavity drops enough to shift the fill-to-pack transition by 0.15–0.30 s. This shift can over-pack thin thread-root sections and reduce tamper-band elongation before failure. Processing targets for non-carbonated beverage closures and sauce caps include melt temperature of 215–235°C, mould coolant inlet between 8°C and 20°C, and hot-runner drop temperatures 5–10°C below the press barrel front-zone setting to prevent polymer degradation at the gate tips. Injection speed should not be reduced below 150 mm/s on 1.2 mm-thick tamper bands; lower speeds produce visible gas entrapment and weak weld lines at the bridge-to-shell junction. Hold pressure is set at 30–45 MPa for 0.7–1.2 s in tools with a single valve gate per cavity; hold beyond 1.5 s is avoided because it increases deformation of the tamper band after ejection. The mould should include water-cooled core pins in the thread root and annular cooling inserts around the valve-gate nozzle; core surface temperatures above 30°C have been associated with thread ovality and leakage complaints on vacuum packaging lines. Food-contact certification follows the same resin-side regulatory framework: 21 CFR 177.1520(c) 3.2a for the United States and Commission Regulation (EU) No 10/2011 for the European Union, including migration testing by the EN 1186 series for aqueous and fatty simulants. Closures for ambient-filled dairy and low-acid sauces are within the normal use envelope; however, DMDA8008 is not recommended for carbonated soft drink or beer closures where sustained internal pressure and environmental stress-cracking resistance measured by ASTM D1693 condition A or B may be lower than required for long shelf life. Published data for this specific configuration is limited, so closure qualification should include a full organoleptic panel and top-load/torque verification on a production-scale capper rather than relying on resin datasheet values alone.

    Before industrial pails and 20-L buckets are moulded from DMDA8008, tool setup must account for the grade’s narrow molecular weight distribution, which reduces warpage but makes melt-temperature control at the check ring decisive for shot-to-shot cushion stability. A 5-L pail with a 2.8–3.2 mm wall and a 20-L bucket with a 3.0–3.5 mm wall are usually produced on 5,000–8,000 kN clamp-force machines with one or two cavities and a three-plate hot runner or cold sprue bush. Barrel temperatures follow a rising profile from 180–200°C in the rear zone to 230–245°C at the front zone; the nozzle is held at 235–250°C. Mould temperature is maintained at 10–20°C with independent cooling channels in the handle side plates and bottom rim area. Injection pressure of 80–110 MPa is applied with a fill time of 1.5–2.5 s for a 5-L pail, while hold pressure of 50–70 MPa is held for 3–6 s to pack the handle and top-rim sections. Inline dosing of a colour masterbatch at the feed throat is limited to 2.0–4.0 wt% for opaque colours; for high-opacity white or red, higher loadings are used only if the masterbatch carrier is a high-flow HDPE or LDPE because a low-flow LLDPE carrier can cause screw slip in the feed zone. Pre-drying is typically not required if pellet surface moisture is below 0.08%; otherwise, a 70°C hopper-air treatment for 1 h is applied. For industrial pails intended for non-aggressive liquid or powder packaging under UN transport regulations, the converter must run drop and stack tests according to the prescribed United Nations Manual of Tests and Criteria and verify compatibility with the specific filling substance. Evidence from HDPE homopolymer grades of similar density indicates that environmental stress-cracking resistance under ASTM D1693 is strongly influenced by moulded-in stress, which is controlled by the 50–70 MPa hold pressure and 10–20°C mould temperature. For food-contact dry goods, the resin must be sourced from a food-grade lot and final article migration measured under EU No 10/2011 or FDA 21 CFR 177.1520.

    When nestable industrial crates are moulded with DMDA8008, side-wall deflection shifts the stacking load limit

    Cold-store distribution totes and nestable dairy crates are produced from DMDA8008 in wall sections from 2.5 mm to 4.0 mm. The processing challenge is not cavity filling but warpage in the long side walls and base ribs after ejection. Mould shrinkage under ASTM D955 for HDPE homopolymer in this density range generally falls between 1.5% and 2.5% in the flow direction and 0.8% to 1.5% in the transverse direction; mould designers therefore offset side-wall features by at least 2.0% before cutting steel. The high-flow melt enters through 8–12 film gates or multiple sequential valve gates, with fill velocities of 150–250 mm/s and hold pressures of 35–50 MPa for 5–10 s depending on wall thickness. Melt temperature is controlled between 225°C and 245°C, while mould coolant enters at 15–25°C on the core side and 10–18°C on the cavity side to remove heat from thick ribs. For sub-zero service down to -20°C, a carbon-black masterbatch with loading that yields 2.0–2.5 wt% carbon black in the final part is used for outdoor and cold-chain durability; carbon-black dispersion is monitored by film cross-section inspection under ISO 11420 or an equivalent internal method. Drop impact at -20°C should be measured by ASTM D2463 or an internal drop protocol on production crates because ductile-to-brittle behaviour varies with tooling and gate placement. In cold-room racking, the side-wall flexural modulus of DMDA8008 in the 1,100–1,400 MPa range according to ASTM D790 is used to calculate deflection under top load; trial campaigns with 1,000 h stacking at 4°C according to ISO 12048 are used to validate creep behaviour. Published data for this specific configuration is limited, so cold-chain qualification should include a 28-day stack test at 4°C and a top-load test at 40°C for distribution to hot climates.

    Material handling trays and dunnage platforms

    DMDA8008 finds use in injection-moulded material handling trays, dunnage platforms, and automotive logistics trays where high-flow fill permits glass-fibre-free rigidity and complex rib geometry. Parts of 4–6 mm nominal wall use cold sprue or hot runner feed with 1.5–2.5 s fill, injection pressure 75–100 MPa, and hold pressure 45–65 MPa for 8–15 s. Mould temperatures of 15–25°C on both core and cavity keep cycle times from 18 s to 35 s on 6,000–12,000 kN machines. The high flow permits low-internal-stress filling of tall ribs, reducing post-mould distortion that causes tray-stacking mismatch in automated conveyor lines. Because these trays are often black for UV protection, carbon black masterbatch at 2.0–3.0 wt% is used; masterbatch above 4.0 wt% can lower weld-line impact strength measured under ASTM D256. Dimensional stability is controlled by allowing 1.5–2.0% mould shrinkage and by specifying a post-mould flatness tolerance of ±0.5 mm over 300 mm according to an internal quality plan. Clean post-industrial regrind may be added up to 15% without exceeding thickness limits, but batch consistency of melt flow ratio should be checked by ASTM D1238 to avoid flow variation that produces short shots in tall ribs.

    When DMDA8008 is used for rigid toy components and thin-wall household storage boxes, the regulatory test burden shifts from food-contact migration to mechanical and chemical safety limits under EN 71 and REACH. Thin-wall storage boxes with snap-fit lids and toy components such as building blocks and sorting trays are injection-moulded from DMDA8008 because the narrow MWD allows fast filling of pin gates and thin ribs. Processing uses melt temperatures of 220–240°C, mould temperatures of 10–20°C, and injection pressures of 60–90 MPa on 1,800–4,000 kN machines. For toys sold in the European Union, the finished component must comply with EN 71-1 mechanical and physical requirements, EN 71-2 flammability, and EN 71-3 migration of certain elements; the extraction limits for antimony, arsenic, barium, cadmium, chromium, lead, mercury, and selenium are defined in mg/kg by material category. For the United States, ASTM F963 applies, including heavy metal extraction and small-part geometry checks. REACH Regulation (EC) No 1907/2006 Annex XVII restrictions on phthalates and PAHs apply to plastic components; the converter should request a REACH declaration from the masterbatch and resin suppliers and avoid adding recycled material unless its origin and historical use are fully documented. Because toy moulds often include living hinges or thin flex elements, the high-flow grade can be processed at the low end of the pressure range to reduce residual stress; however, hinge endurance should be tested with 5,000–10,000 cycles on production samples because published data specific to DMDA8008 living hinges is limited.

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