| HS Code | 874361 |
| Melt Flow Rate | 8.0 g/10 min |
| Density | 0.955 g/cm3 |
| Tensile Yield Strength | 28 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1150 MPa |
| Notched Izod Impact Strength | 50 J/m |
| Vicat Softening Point | 126 °C |
| Brittleness Temperature | -70 °C |
| Shore D Hardness | 65 |
| Environmental Stress Cracking Resistance | >1000 h |
| Water Absorption | <0.01% |
| Melting Point | 135 °C |
As an accredited CHN Energy Ningxia Coal HDPE 8008 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | CHN Energy Ningxia Coal HDPE 8008 comes in 25 kg PP woven bags, also available in 1,000 kg jumbo bags. |
| Container Loading (20′ FCL) | Container loading: CHN Energy Ningxia Coal HDPE 8008 in 20' FCL, 25kg bags, 18MT net, palletized, shrink-wrapped for export. |
| Shipping | CHN Energy Ningxia Coal HDPE 8008 is a non-hazardous solid polymer, typically shipped in 25 kg PP woven bags or 1,000 kg jumbo bags, palletized and stretch-wrapped. Transport in clean, dry containers or trucks. Store cool, dry, ventilated, away from moisture, heat, and direct sunlight. |
| Storage | Store CHN Energy Ningxia Coal HDPE 8008 in a cool, dry, well-ventilated warehouse. Keep original bags sealed and palletized, off the floor, away from direct sunlight, moisture, heat, ignition sources, and strong oxidizers. Avoid prolonged UV exposure, high temperatures, crushing, and contamination. Use first-in, first-out rotation; keep containers labeled; follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Store in dry, ventilated conditions, away from direct sunlight; typical shelf life is 24 months in unopened original packaging. |
Within returnable injection moulded transit packaging, CHN Energy Ningxia Coal HDPE 8008 is handled as a material with nominal density 0.956 g/cm³ and melt flow rate 7.6 g/10 min at 190 °C and 2.16 kg load, determined in accordance with ISO 1183-1:2019 and ISO 1133-1:2022. On bottle crate and dunnage tray lines, barrel set points are held between 190 °C and 220 °C, with the nozzle at 200–210 °C and the mould surface at 15–25 °C. Injection machines are specified with clamp force from 12,000 kN to 25,000 kN for multi-cavity crate tools, using screws with L/D ratios of 20:1 to 24:1 and compression ratios of 2.5:1 to 3:1. The screw advance is profiled at 80–150 mm/s mid-stroke to avoid jetting in thick bosses. Holding pressure is controlled in the range 60–80 MPa; moulded sections of 4 mm require hold times of 8–12 s to reach gate seal, while 6 mm ribbed sections are held for 14–20 s. The terminal articles are returnable soft drink crates, fruit bins, and logistics dunnage trays, where dimensional stability is checked after 24 h at 23 °C under ISO 294-4; mould shrinkage is typically recorded at 1.8–2.2% in flow and 1.7–2.1% cross-flow.
Regrind incorporation is limited to 20 wt% of clean, dry skeleton material in this sector because higher internal recycle fractions lower the notched Charpy impact value measured by ISO 179-1/1eA and broaden the gate-seal window. Drying is not needed when silo storage is closed and ambient relative humidity is below 60%; when regrind is stored in open bins at relative humidity above 60%, pre-drying at 60 °C for 2 h is applied to reduce surface splay. On production-scale machines, failure modes include gas entrapment at rib intersections, flow lines radiating from ejector bosses, and warpage caused by non-uniform cooling in the base grid. These defects are addressed by reducing melt temperature in the front zone to 205 °C, increasing screw back pressure to 0.8–1.2 MPa, and balancing cooling circuits to hold a core/cavity temperature differential below 5 °C.
Pail-grade conversion of HDPE 8008 is qualified primarily by environmental stress crack resistance rather than short-term mechanical strength. For non-food industrial pails of 5 L to 25 L, the body wall is moulded at 1.8–2.5 mm thickness and the material is processed at melt temperatures of 200–225 °C with mould temperatures of 15–20 °C. Ageing resistance is assessed under ASTM D1693-15 Method B, using 10% Igepal CO-630 solution at 50 °C. Weld lines formed at the handle ears and bottom corners are the governing defect sites. Pails with integral bail ears are produced on single or dual cavity tools with central annular sprue gates; the injection pressure is 80–110 MPa and hold pressure 60–75 MPa. Cooling time for 2.2 mm walls is set at 18–25 s to reach ejection below 65 °C part surface temperature, reducing corner distortion. When pails are filled with detergent or mild oxidiser solutions, stress crack initiation is accelerated by moulded-in residual stress from excessive packing, particularly in the gate zone and under the handle ears. Gate pressure decay is monitored by recording pressure at switchover in every cycle; deviation above 5 MPa indicates check-ring wear or nozzle clogging. Because published datasheet values for ESCR of this specific grade are limited, acceptance criteria are established by converter trials against the packaged matrix. Terminal products include detergent pails, lubricant pails, and paint pails where UN certification for dangerous goods is not required. If dangerous goods packaging is required, the finished pail must pass stacking and drop tests specified in the applicable UN Model Regulations Chapter 6.1 and ADR/RID Chapter 6.1.
Food-contact conversion of HDPE 8008 for thin-wall dairy tubs is controlled under Regulation (EU) No 10/2011 as amended and 21 CFR 177.1520. The polymer itself falls under the class of ethylene homopolymers covered by the applicable positive list, but the finished article must satisfy overall migration and specific migration requirements for the intended food simulant. The process window is severe because wall thickness ranges from 0.25 mm to 0.50 mm and the flow length-to-wall-thickness ratio can exceed 200:1. Melt temperature is raised to 215–235 °C, while mould temperature is held at 8–18 °C to freeze residual stress quickly and permit cycle times of 4.5–8 s. Injection speed is set at 300–600 mm/s screw advance on accumulator machines; clamp force per cavity is typically 80–150 kN. In 0.30 mm walls, the injection phase is reduced to 0.2–0.4 s and the holding pressure is restricted to 35–50 MPa to prevent core deflection and gate-stringing.
| Control Parameter | Standard or Regulation | Typical Test Condition | Numerical Limit |
|---|---|---|---|
| Overall migration in aqueous simulant | EN 1186-1:2002 | simulant A, 40 °C, 10 d | 10 mg/dm² |
| Overall migration in acidic simulant | EN 1186-1:2002 | simulant B, 40 °C, 10 d | 10 mg/dm² |
| Overall migration in fatty simulant | EN 1186-1:2002 | simulant D1, 40 °C, 10 d | 10 mg/dm² |
| Zinc specific migration | Regulation (EU) No 10/2011 | EN 13130-1:2004 | 5 mg/kg |
Terminal articles include yogurt cups, dessert cups, dairy lids, and portion packs. On high-cavitation stack moulds, cycle-to-cycle mass variation is held within ±0.15% to maintain uniform wall thickness; any cavity exceeding this deviation is inspected for nozzle tip wear, hot-runner heater failure, or gate freeze delay.
Closure production lines using Grade 8008 favour high-cavitation tools with 48, 64 or 96 cavities, hot runner valve gates, and cold base plates with conformal cooling. The melt is injected at 215–235 °C through 16 to 24 mm screw diameters with an L/D ratio of 20:1; the mould surface is held at 10–20 °C to limit closure ovality and bridge distortion. Tamper-evident closures require a slot bridge thickness of 0.12–0.18 mm, which is achieved by holding pressure of 55–70 MPa and a cushion of 2–4 mm. Cycle times of 5.5–7.5 s are empirical limits observed on 72-cavity tools because demoulding forces and hot-runner flow imbalance produce bridge-thickness variation above 0.03 mm when cycle times are shortened further. Application torque is checked on line with a torque meter according to ASTM D2063-12; closures are aged for 24 h at 23 °C and evaluated for minimum removal torque. Terminal products are non-carbonated bottled water closures and carbonated soft drink closures with PCO neck standards. Compliance with 21 CFR 177.1520 applies for food contact, and Regulation (EU) No 10/2011 applies where the closures are exported to EU markets.
In closure production, the main failure modes are gate voids at the bridge, incomplete slit perforation, and ovality greater than 0.2 mm measured on the closure outer diameter. These are corrected by setting the valve pin delay 0.1–0.3 s, profiling decompression to 3–5 mm, and adjusting coolant flow to keep cavity-to-cavity surface temperature spread below 4 °C. Additive packages containing silicone-based mould release or slip agents are limited because excess slip compounds at levels above 0.5 wt% can raise coefficient of friction variability and reduce print adhesion on the top panel; where printing is required, corona treatment at 38–42 mN/m surface tension is applied after moulding.
In paint pail lid moulding, the centre-gated disc with an outer sealing seat is sensitive to differential radial shrinkage. With a melt flow rate of 7.6 g/10 min, the material can fill a 310 mm diameter lid at 2.0–2.5 mm thickness from a central sprue when injection pressure is 70–90 MPa and melt temperature is 210–225 °C. Three-plate tools with four or six direct gates are preferred where concentricity of the sealing seat must be held below 0.35 mm. However, added gates generate weld lines in the outer flange; these weld lines reduce Charpy impact strength measured by ISO 179-1/1eA by 20–35% relative to the gate-free zones when tested at -20 °C. The sealing seat is therefore designed with a minimum radius of 0.3 mm and a wall-thickness transition no steeper than 1:1 to avoid notch effects.
Mould shrinkage on pail lids is measured after 48 h at 23 °C under ISO 294-4; radial shrinkage across the disc is controlled to 1.6–2.0% by holding pressure 55–75 MPa and holding time 10–16 s. When the gasket groove is overpacked, the lid can exhibit cupping greater than 0.8 mm measured across the seating plane, and this is corrected by reducing packing in the outer zones through sequenced valve-gate opening. Terminal articles include snap-on and tear-open paint pail lids from 1 L to 20 L, where solvent compatibility is confirmed by storing at 40 °C for 14 d in the actual packaged paint formulation.
Competitive CHN Energy Ningxia Coal HDPE 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
Flexible payment, competitive price, premium service - Inquire now!