| HS Code | 567113 |
| Density | 0.939 g/cm³ |
| Melt Index | 0.50 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 19.3 MPa |
| Tensile Strength At Break | 24.1 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 758 MPa |
| Environmental Stress Crack Resistance Escr | >1000 h |
| Vicat Softening Temperature | 120°C |
| Brittleness Temperature | -70°C |
| Shore D Hardness | 60 |
| Carbon Black Content | 2.5% |
| Water Absorption | <0.01% |
| Thermal Conductivity | 0.35 W/m·K |
| Dielectric Constant | 2.3 |
| Volume Resistivity | >1e16 ohm·cm |
As an accredited NOVA Chemicals Sclair MDPE 8406 BK factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | NOVA Chemicals Sclair MDPE 8406 BK is packaged in sealed 25 kg polyethylene bags, with 40 bags per pallet. |
| Container Loading (20′ FCL) | NOVA Chemicals Sclair MDPE 8406 BK loaded in 20′ FCL: palletized 25 kg bags, shrink-wrapped, dry container, secure stowage, within weight limits. |
| Shipping | NOVA Chemicals Sclair MDPE 8406 BK ships as non-hazardous black medium-density polyethylene resin pellets in sealed bags, octabins, or bulk containers. It is not regulated by DOT, IMDG, or IATA; no UN number, hazard class, or placards are required. Keep dry and protected from UV and ignition sources. |
| Storage | Store NOVA Chemicals Sclair MDPE 8406 BK in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original containers closed and intact, protect from moisture, dust, and UV exposure, and avoid prolonged elevated temperatures. Use clean handling equipment, observe good housekeeping, and follow the supplier’s SDS and local regulations. |
| Shelf Life | Shelf life is typically indefinite when stored in a cool, dry, well-ventilated area away from direct sunlight and heat sources. |
On a three-arm carousel rotational molding line, Sclair MDPE 8406 BK is charged as a pre-pigmented black powder with a target particle size distribution passing through a 35-mesh screen. The black pigment package alters infrared absorption, so mold surface pyrometer readings typically lead internal air temperature by 5 °C to 8 °C during the first 12 min of the heating cycle. Large seamless fertilizer and industrial water tanks molded from this grade are designed with wall sections of 5.0 mm to 12.7 mm, depending on service pressure and tank height. The lower melt flow index of medium density polyethylene, when compared with LLDPE rotomolding grades, extends the sintering window but demands a higher peak internal air temperature, normally 195 °C to 215 °C, to eliminate micro-voids at particle boundaries. Mold rotation ratios on cylindrical tanks are set between 3:1 and 5:1 primary-to-secondary, with a full 360° rotation every 45 s to 75 s. If the rotation is interrupted or the vent tube is clogged by powder carryover, oxygen in the cavity is depleted and under-sintered areas form near the top manway boss. Production records from carousel lines indicate that pinhole defect clusters at the parting line are almost always associated with vent tubes shorter than 40% of the mold’s longest axis or with powder that has accumulated moisture above 0.05 wt%. The latter requires pre-drying at 60 °C for 4 h when bulk powder is stored in unheated warehouses. Demolding is initiated only after the internal air temperature falls below 90 °C and the mold surface temperature drops below 80 °C. Forced air cooling at 4 °C/min to 8 °C/min between 120 °C and 80 °C minimizes warpage at the manway opening; water mist is delayed until the mold surface is below 100 °C because early quench cracking has been observed around brass inserts.
Regulatory acceptance for agricultural chemical containment is evaluated less by short-term tensile yield than by environmental stress cracking resistance, permeation rate, and chemical attack on the amorphous phase. The seamless wall produced by rotational molding eliminates weld lines, but chemical compatibility remains the limiting design criterion. ASTM D543-20 immersion testing should be carried out with the intended fertilizer or pesticide concentrate at 40 °C and 60 °C for 90 days, with tensile yield retention measured per ASTM D638-22. Sclair MDPE 8406 BK generally exhibits higher ESCR under ASTM D1693-15 Condition B than HDPE rotomolding grades of comparable melt flow, because the lower crystallinity reduces craze propagation. However, the current lot certificate must be checked for actual ESCR values because additive package changes affect failure time by more than 200 h in some lots. Concentrated aromatic hydrocarbons are outside the recommended service envelope: they plasticize the amorphous phase and can reduce flexural modulus by more than 20% within 30 days of immersion. Chlorinated solvents are similarly excluded. For tank walls thicker than 6.35 mm, permeation rates decline linearly with wall thickness, but thermal expansion stress at large flat sidewalls increases, requiring external stiffeners or molded ribs. Secondary containment bund walls molded from the same grade are usually designed with a 110% volumetric capacity of the primary tank, and hydrostatic testing is carried out per ASTM D1998-15 where applicable.
Pre-pigmented black powder supplied as 8406 BK eliminates the masterbatch dilution step in kayak and canoe production, reducing batch-to-batch color drift in multi-cavity rotational molding cells. Hulls are commonly molded as double-shell parts with a foamed core inserted after the outer skin has sintered. The outer skin is charged first at a thickness of 1.5 mm to 3.0 mm, followed by a foam shot and an inner skin of 2.0 mm to 4.0 mm. Peak internal air temperature for the second skin is held between 190 °C and 205 °C to fuse the inner layer without collapsing the foam core. If the inner skin drops below 185 °C, delamination is detectable by tap-testing and by scanning acoustic microscopy. Low-temperature impact resistance of the hull is assessed under ISO 6603-2 at -20 °C, while tensile yield and elongation at break are reported per ASTM D638-22. Rotomolding shops using 8406 BK for recreational hulls record that black outer skins reach surface temperatures above 65 °C in direct sun, which can cause local creep at roof-rack contact points if the wall is thinner than 4.0 mm. Structural inserts for handles and seat mounts must be isolated from the hull skin with polyethylene gaskets to avoid notch-induced cracking in the rigid frame region.
On four-arm carousel machines with a fixed dwell angle, a cycle-time reduction below 18 minutes in the first arm shifts the sintering condition from a fully recrystallized spherulitic morphology to a particle-boundary morphology. Under-cured MDPE parts frequently pass visual inspection but fail low-temperature impact testing because particle boundaries remain as weak points. Differential scanning calorimetry per ASTM D3418-21 at a heating rate of 10 °C/min shows a low-temperature shoulder on the main melting endotherm when residual un-melted particles are present. The black pre-pigmentation in 8406 BK reduces the time needed to reach the melting plateau compared with natural PE by 10% to 15%, but process engineers cannot use this as a justification to cut oven residence time below the point where internal air temperature reaches 195 °C. A narrow processing window exists: internal air temperature at peak should be 195 °C to 215 °C, and the time above 180 °C should be at least 8 minutes for 6.35 mm walls. If the peak exceeds 225 °C, oxidative degradation produces carbonyl species that can be detected by FTIR at 1740 cm⁻¹ and lowers impact retention by more than 30%. The use of a non-contact pyrometer calibrated against an internal air probe is mandatory because mold surface emissivity shifts during heating as the powder fuses from a rough layer to a smooth melt. Published process guidelines for medium density polyethylene rotomolding grades on carousel lines recommend that the cooling rate between 120 °C and 80 °C be kept to 4 °C/min to 8 °C/min.
| Process variable | Typical range on production-scale carousel machines | Critical defect threshold |
|---|---|---|
| Oven setpoint | 260 °C to 315 °C | Above 315 °C surface oxidation and carbonyl formation |
| Peak internal air temperature | 195 °C to 215 °C | Below 185 °C incomplete sintering and pinholes |
| Time above 180 °C | 8 min to 14 min for 6.35 mm walls | Below 8 min particle-boundary failure |
| Demolding mold surface temperature | 80 °C maximum | Above 95 °C warpage at bosses and manway rims |
| Cooling rate from 120 °C to 80 °C | 4 °C/min to 8 °C/min | Above 10 °C/min risk of quench cracking |
| Primary-to-secondary mold rotation ratio | 3:1 to 5:1 | Below 2:1 non-uniform wall thickness distribution |
Outdoor playground structural panels molded from 8406 BK are exposed to UV-A and UV-B radiation, rain, freeze-thaw cycles, and vandalism. The pre-compounded carbon black package in the BK grade provides UV screening only if the black pigment is dispersed as agglomerates smaller than 20 µm. Dispersion quality is inspected by microtome cross-section under transmitted light microscopy, using ISO 18553:2002 Method A as the test protocol. Large agglomerates above 100 µm act as stress risers and can reduce elongation at break by over 40% in tensile tests performed per ASTM D638-22. Procurement specifications for playground equipment in the European Union require accelerated weathering per ISO 4892-2:2013 Method A with a xenon-arc source, typically 2000 h exposure, followed by impact testing per ISO 6603-2 and visual assessment for chalkiness. The black surface reaches 75 °C in full sun, so creep modulus under ISO 899-2 should be verified for structural members subject to handrail loading. Because 8406 BK is a medium density polyethylene, its flexural modulus is lower than HDPE; structural designers compensate with thicker ribs or metal inserts. The material should not be machined after molding in a way that removes the outer carbon-black-rich skin, because the interior may have lower UV stability.
When 8406 BK is specified for mining concentrate bins, the selection is driven by impact fatigue resistance rather than dry abrasion performance. The application is not a dry abrasion service; MDPE has lower wear resistance than UHMWPE or HDPE, and sliding wear of the walls under quartz-bearing slurries can exceed 0.5 mm/year in continuous duty. Published data for abrasion rates of 8406 BK in quartz-bearing slurry service is limited; wear trials on a production-scale bin are required before specifying minimal wall thickness. The decision to use 8406 BK rests on its impact strength and ability to form seamless corners with thick walls. Bins are typically molded with wall thickness from 6.0 mm to 10.0 mm and external steel cradles. Electrostatic charge accumulation is a significant constraint: carbon black in the BK formulation is not loaded at levels sufficient to make the material conductive, and surface resistivity may remain above 1×10¹² Ω under IEC 61340-5-1. When handling combustible mineral dusts, rotomolded bins must be grounded via embedded metal plates, and fill lines must be inerted. The use of 8406 BK for food-contact service is not assumed; FDA 21 CFR 177.1520 compliance should be confirmed for each lot when indirect food contact is regulated.
Septic tanks and underground stormwater chambers rotomolded from 8406 BK are often produced with wall thicknesses from 6.35 mm to 12.7 mm. The thicker cross section increases the time required for the inner surface to reach the melt plateau, and the molding cycle is dominated by heat transfer through the powder bed. Ultrasonic thickness mapping per ASTM E797 on multi-cavity tools shows that corner wall thickness can be 30% to 50% lower than mid-wall thickness when the mold is charged with a single dry powder shot. This variation forces the processor to increase the charge weight until the thinnest corner meets the minimum design wall, which in turn creates thicker mid-walls and longer cooling times. Cooling is the critical process constraint for thick underground chambers: the cooling rate between 120 °C and 80 °C should be held to 4 °C/min to 6 °C/min, and demolding is delayed until the mold surface falls below 80 °C. If cooling is accelerated above 8 °C/min, differential shrinkage across the wall thickness produces residual stress that can later relax under soil load, causing detectable deformation at the access riser. The design of underground chambers must also include buckling resistance under saturated soil load; long-term creep modulus testing under ISO 899-2 is used to confirm deflection limits. The following test matrix is commonly applied to first-article qualification.
| Qualification property | Test method | Required condition |
|---|---|---|
| Tensile yield and elongation at break | ASTM D638-22 | Current lot certificate values; no yield drop after 90-day chemical immersion |
| Environmental stress cracking resistance | ASTM D1693-15 Condition B | Failure time per purchaser specification; confirm current lot |
| Low-temperature impact resistance | ISO 6603-2 | No brittle puncture at -20 °C |
| Accelerated weathering | ISO 4892-2:2013 Method A | No cracking or chalkiness after specified exposure |
| Chemical resistance | ASTM D543-20 | No visible attack; tensile retention above purchaser minimum |
| Electrostatic surface resistivity | IEC 61340-5-1 | Grounding required if above 1×10¹² Ω |
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