| HS Code | 753549 |
| Density | 0.935 g/cm³ |
| Melt Index | 0.7 g/10 min |
| Melting Point | 125 °C |
| Vicat Softening Point | 111 °C |
| Tensile Strength At Yield | 19 MPa |
| Tensile Strength At Break | 30 MPa |
| Elongation At Break | 800% |
| Flexural Modulus | 800 MPa |
| Environmental Stress Crack Resistance | 1000 h |
| Low Temperature Brittleness | -70 °C |
| Hardness | 55 Shore D |
| Haze | 10% |
| Gloss | 60 |
| Dart Drop Impact | 250 g |
| Elmendorf Tear Strength Md | 300 g |
| Elmendorf Tear Strength Td | 400 g |
| Coefficient Of Friction | 0.2 |
As an accredited NOVA Chemicals Sclair LMDPE 14G factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | NOVA Chemicals Sclair LMDPE 14G is supplied in 25 kg moisture-resistant polyethylene bags, stacked on pallets for industrial handling and storage. |
| Container Loading (20′ FCL) | Loaded in a 20-foot FCL dry container: palletized 25 kg bags of Sclair LMDPE 14G, ambient conditions, secured for transport. |
| Shipping | NOVA Chemicals Sclair LMDPE 14G is shipped as non-hazardous polyethylene resin pellets, typically in 25 kg bags on pallets or in bulk trucks/railcars. Keep containers closed, dry, and protected from sunlight and heat; follow the SDS and local regulations. Not classified as dangerous goods for transport. |
| Storage | Store NOVA Chemicals Sclair LMDPE 14G resin in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and open flames. Keep original packaging closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and physical damage to bags or containers. Use good housekeeping and follow the manufacturer’s SDS and local storage regulations. |
| Shelf Life | Shelf life: typically two years from manufacture when stored unopened in original packaging, cool and dry, protected from UV and moisture. |
Injection moulding of tamper-evident beverage closures with Sclair LMDPE 14G is governed by the interaction of torque retention, slow crack growth resistance, and food-contact migration limits. The lot should be verified against a nominal density of 0.934 g/cm³ by ASTM D1505 and a nominal melt flow rate of 4.0 g/10 min by ASTM D1238 at 190°C/2.16 kg. A reciprocating-screw injection moulding machine with an 18:1 to 22:1 L/D screw, a compression ratio of 2.4:1 to 2.8:1, and a shut-off nozzle is used. Barrel temperatures are set from 190°C at the feed zone to 215°C at the metering zone and nozzle; hot-runner valve-gate tips are held at 215°C to 225°C to avoid premature gate freeze-off in a 0.9 mm to 1.2 mm wall. Cavity pressure at transfer should reach 30 MPa to 35 MPa, with clamp force calculated from the projected area of the closure array at this pressure. A white closure masterbatch is usually added at 2 wt% to 4 wt%; antistatic, slip, and antiblock additives are avoided unless the package design has been tested under ASTM D2063 for removal torque retention and ASTM D3198 for application and removal torque. Regrind from clean runner and rejects is limited to 20 wt% of the shot because higher fractions shift the cap dimensional recovery after storage and increase variation in ESCR as evaluated by ASTM D1693, Condition B. Terminal articles are 28 mm and 38 mm tamper-evident closures for still water, carbonated soft drinks, UHT dairy, and aseptically filled sauces.
| Regulation/standard | Test method or clause | Condition or limit |
|---|---|---|
| FDA 21 CFR 177.1520(c) | Olefin polymer specification; n-hexane extractable fraction | 50°C condition; condition-of-use matrix per 21 CFR 176.170(c) |
| EU Regulation (EC) No 10/2011 | Annex III overall migration; Annex I specific migration | ≤ 10 mg/dm² |
| China GB 9685-2016 | Positive list for additives in PE | Only listed additives at permitted maximum use levels |
| Japan MHLW Notification No. 370 | Polyolefin finished-article test | Cd ≤ 100 µg/g; Pb ≤ 100 µg/g |
Thin-wall storage totes and toy bins moulded from Sclair LMDPE 14G are filled with an injection speed profile that reaches 90% of maximum machine velocity within 0.3 s to 0.5 s, then reduces to 45% to 55% before transfer to packing. For nominal wall sections of 1.5 mm to 2.0 mm, the total fill time is kept below 1.5 s; if fill time exceeds this threshold at a mould coolant temperature of 10°C to 25°C, the frozen skin layer prevents adequate packing and increases differential shrinkage. Holding pressure is set at 45 MPa to 60 MPa and held for 6 s to 10 s until the gate freezes. The tool should provide 0.5° to 1.0° draft on ribbed surfaces and an ejector plate with ejector pins positioned on long side walls. White or light-coloured masterbatch loading is maintained at 2 wt% to 3 wt%; filler masterbatches above 5 wt% increase notched Izod brittleness under ASTM D256 and are not suitable for drop-tested toy parts under EN 71-1:2014+A1:2018. If the moulded article is classified as a toy or childcare article, chemical migration is determined under EN 71-3:2019, and the presence of restricted phthalates is evaluated under EU REACH Annex XVII entries 51 and 52. Food-contact storage containers additionally require lot-specific positive-list verification under EU Regulation (EC) No 10/2011 and FDA 21 CFR 177.1520(c). Terminal products include stackable storage totes with snap lids, toy bins, hangers, and modular drawer systems.
Open-head industrial pails and shipping containers converted from Sclair LMDPE 14G are normally moulded on 250 t to 500 t machines with a melt temperature of 200°C to 225°C and a mould coolant inlet of 8°C to 20°C. A 20 L pail with a 2.5 mm to 3.0 mm wall uses a shot weight of 1.1 kg to 1.3 kg and a cycle time of 35 s to 45 s. The screw speed is held at 40 rpm to 60 rpm with back pressure of 0.5 MPa to 1.0 MPa to avoid uncontrolled shear heating. UV-stabilized outdoor formulations are achieved by adding a hindered amine light stabilizer masterbatch at 1.5 wt% to 2.5 wt%; the tensile properties after pigment addition are rechecked under ASTM D638, and ESCR is rechecked under ASTM D1693, Condition B, because certain inorganic pigments can nucleate the polyethylene and reduce slow crack growth resistance. Clean in-house regrind is limited to 30 wt%; if regrind is stored at relative humidity above 60%, the flake must be dried at 70°C for 1 h to 2 h before processing. Transport certification for hazardous goods is based on 49 CFR 178.603 for the UN drop test, 49 CFR 178.604 for leakproofness, and 49 CFR 178.606 for stacking; equivalent provisions under IMDG Code and ISO 16101:2004 apply for sea and international shipments. Terminal articles are 5 L to 25 L open-head pails for water-based coatings, food ingredients, industrial lubricants, and solid chemical premixes.
For distribution crates and totes moulded from Sclair LMDPE 14G, the critical design parameter is not short-term tensile strength but the ductile-to-brittle behaviour at −20°C after repeated stacking. A 45 L ventilated crate with 2.0 mm to 3.0 mm wall is run on a 500 t to 800 t machine with melt temperature 210°C to 240°C and mould temperature 10°C to 25°C. Gate locations are placed in the base corners, not along the upper rim, to move weld lines away from the stacking lugs. Holding pressure is 50 MPa to 60 MPa with cooling time 18 s to 25 s. Clean unfilled regrind is limited to 15 wt%; calcium carbonate masterbatch above 5 wt% raises the low-temperature impact failure rate under ISO 6603-1 and is rejected for cold-chain return logistics. Rib thickness is held at 60% to 70% of the adjacent wall to limit sink marks, and the base should include at least 4 ground-contact pads to distribute pallet rack point loads. Stacking performance is evaluated according to ISO 12048 for complete, filled transport packages; creep at elevated warehouse temperatures is evaluated using lot-specific Vicat softening data under ASTM D1525, and load-bearing designs should not assume room-temperature modulus above 40°C. Food-contact use for meat or dairy trays requires EU Regulation (EC) No 10/2011 and FDA 21 CFR 177.1520(c) positive-list verification. Terminal articles include beverage crates, bakery trays, automotive parts bins, and agricultural harvest totes.
Sheet extrusion of Sclair LMDPE 14G for returnable dunnage trays and separator sheets is carried out on a 75 mm to 120 mm single-screw extruder with a 30:1 L/D barrier screw and a 2.5:1 compression ratio. Barrel temperatures are profiled from 180°C at the feed throat to 215°C at the die adapter; a 40/60/80 mesh screen pack removes unmelt and foreign particles, while melt pressure before the screen pack is kept below 25 MPa to avoid excessive residence time. A flex-lip sheet die with 1.4 m to 2.0 m working width delivers a sheet of 2 mm to 4 mm through a three-roll stack maintained at 60°C to 80°C. The sheet is thermoformed at a surface temperature of 130°C to 150°C using plug-assist tools; because LMDPE has a narrow sag window above the crystalline melting region, zoning in ceramic or quartz heaters must be validated with an infrared pyrometer before start-up. Clean edge trim regrind can be reintroduced at 30 wt%; regrind with paper, adhesive, or moisture above 0.05% is excluded because it creates microvoids visible as delamination in thermoforming. The finished non-food dunnage must comply with the heavy metal sum limit of 100 mg/kg for lead, cadmium, mercury, and hexavalent chromium under EU Packaging and Packaging Waste Directive 94/62/EC, Annex II, and automotive interior horizontal surfaces must be verified under FMVSS 302 burn-rate testing. Terminal products include custom dunnage trays, returnable rack liners, and separator layers between stamped metal components.
Rotational moulding of Sclair LMDPE 14G requires grinding to a 35-mesh powder with a dry-flow value below 30 s/50 g; otherwise multi-axial wall thickness variation becomes unacceptable in corners. Oven air temperature is typically 260°C to 290°C, with peak internal air temperature at 200°C to 210°C for 5 min to 8 min. Published data for this specific grade in rotomoulding is limited, so the converter must run a wall-thickness validation trial before serial production because the 4.0 g/10 min melt flow rate coalesces faster than typical rotomoulding MDPE and can generate inner-wall porosity if peak internal air temperature is exceeded. Outdoor utility tanks should be dry-blended with 0.5 wt% to 1.0 wt% HALS UV stabilizer masterbatch; potable-water tanks require NSF/ANSI 61 extraction testing on the finished article. Terminal products are 20 L to 200 L utility tanks and secondary containment bunds for stationary storage.
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