| HS Code | 802868 |
| Productname | NOVA Chemicals Sclair MDPE 13J7 |
| Polymertype | Medium Density Polyethylene (MDPE) |
| Density | 0.939 g/cm³ |
| Meltindex | 0.35 g/10 min (190°C/2.16 kg) |
| Meltflowratio | 100 |
| Tensilestrengthatyield | 20 MPa |
| Tensilestrengthatbreak | 30 MPa |
| Elongationatbreak | 800% |
| Flexuralmodulus | 900 MPa |
| Vicatsofteningpoint | 115 °C |
| Escr | >1000 h (100% Igepal) |
| Lowtemperaturebrittleness | -70 °C |
| Hardnessshored | 60 |
| Waterabsorption | <0.01% |
| Thermalconductivity | 0.35 W/m·K |
| Dielectricconstant | 2.3 |
| Volumeresistivity | >10^16 ohm·cm |
| Coefficientoflinearthermalexpansion | 1.2 × 10^-4 /°C |
As an accredited NOVA Chemicals Sclair MDPE 13J7 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packed in 25 kg moisture-barrier bags, palletized for safe industrial storage and handling. |
| Container Loading (20′ FCL) | NOVA Chemicals Sclair MDPE 13J7 is loaded in a 20-foot FCL container, palletized in bags, kept dry and securely stowed. |
| Shipping | NOVA Chemicals Sclair MDPE 13J7 is a non-hazardous polyethylene resin shipped as pellets in 25 kg moisture-barrier bags on pallets, or in bulk trucks/railcars. Keep dry, clean, and protected from UV/heat; avoid contamination and static buildup. Store in a cool, ventilated area and follow local regulations. |
| Storage | Store NOVA Chemicals Sclair MDPE 13J7 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep containers closed and clearly labeled to prevent moisture, contamination, and dust accumulation. Avoid prolonged storage near incompatible materials, and follow local regulations and supplier safety data. |
| Shelf Life | Shelf life is typically 24 months when stored cool, dry, well-ventilated, and away from direct sunlight and ignition sources. |
Rotomolded chemical containment uses NOVA Chemicals Sclair MDPE 13J7 as a mid-density wall-stock resin with a nominal density of 0.937 g/cm³ under ASTM D792-20 and a melt index of 7.0 g/10 min under ISO 1133-1:2022, specified where the combination of environmental stress-crack resistance and low-temperature ductility is required. The governing standards for this downstream segment are ASTM D1998-21 for upright polyethylene storage tanks and EN 13575:2012 for above-ground thermoplastic tanks; chemical compatibility is screened by immersion testing under ASTM D543-21, and environmental stress-cracking resistance is characterized under ASTM D1693-21 as a first-article requirement. The formulation for chemical containment is based on 100 parts by weight of pulverized 13J7, 2.5-3.5 wt% HALS-based UV stabilization masterbatch in an LLDPE carrier, 1.0-2.0 wt% carbon black masterbatch where black outer walls are specified, and up to 10 wt% internally screened post-industrial rotomolding regrind derived from the same 13J7 formulation. The downstream production sequence begins with dry blending in a ribbon blender for 12-15 min at 20-30 rpm, followed by charging into cast-aluminum molds with wall-temperature sensors; biaxial rotation is run at a ratio between 3:1 and 4:1, with oven setpoints of 280-300 °C, a peak internal air temperature of 215-230 °C, and a post-fusion heating period of 6-12 min depending on wall thickness. Forced-air cooling from 230 °C to a demold temperature of 70-80 °C at 8-15 °C/min reduces flat-bottom warpage. When cold-stored powder is moved into a humid plant, a 60 °C air purge for 2 h is applied to eliminate surface condensation before charging. Terminal articles include vertical storage tanks from 5,000 L to 20,000 L, bunded pallets with 110% secondary containment capacity, and rectangular IBC outer shells.
On production-scale multi-arm carousel machines, flat-bottom tanks with capacities above 10,000 L show higher reject rates when mold parting-line cold zones localize thickening at the base radius; thermal imaging after demolding is used to detect temperature asymmetry, and the preferred correction is to raise the rotation ratio from 3:1 to 4:1 rather than to elevate oven temperature beyond 300 °C.
Potable water and wastewater components are regulated by NSF/ANSI/CAN 61 in North America and by AS/NZS 4020:2005 in Australia and New Zealand; the relevant test extracts the molded wall at pH 5 and pH 8, with heavy-metal migration and organic leachates compared against health-based limits. Sclair MDPE 13J7 is used in this segment at 100 parts by weight with 0 wt% post-consumer recyclate and 0-1.5 wt% water-contact-compliant colorant masterbatch to minimize contaminant contribution from the formulation side. The rotomolding process is set lower than chemical tank molding—oven setpoint 270-290 °C, peak internal air temperature 210-220 °C, post-fusion hold 10-15 min—to reduce oxidative volatile byproducts that could increase extractable organic carbon. The mold is rotated at a 3:1 speed ratio, and the article is demolded at 75 °C or below before being held for 48 h at ambient warehouse conditions to dissipate short-chain volatile species. Terminal products include 500-10,000 L potable water storage tanks, submersible pump chambers, stormwater hydrodynamic separator shells, and effluent distribution boxes.
Wall thickness at threaded inserts and flanged outlets is maintained above 8 mm because thinner sections relax after demolding and produce leakage paths during hydrostatic testing; zinc-free mold release is specified to avoid zinc contamination in extraction testing under NSF/ANSI/CAN 61.
For agricultural chemical and animal husbandry fluid contact, Sclair MDPE 13J7 is selected for resistance to pH-shifted agrochemical solutions and repeated hydraulic loading rather than for stiffness. Qualification for this segment is governed by ISO 175:2010 immersion testing, with mass change in a representative agrochemical simulant specified below 1.5% after 28 days at 23 °C; tensile retention is checked under ASTM D638-22 Type IV at 50 mm/min, and published data for this specific 13J7 simulant combination is limited, so first-article qualification is conducted with the end-use agrochemical mixture. The formulation is composed of 96-98 wt% 13J7, 2.0-3.5 wt% UV-stabilized colorant masterbatch—commonly carbon black at 2.5 wt% for outdoor service—and 0-10 wt% internally generated regrind where the tank is not subject to potable-water extraction limits. Processing uses fabricated steel or cast aluminum rotational molds with wall thicknesses of 6-10 mm, oven setpoint 280-300 °C, peak internal air temperature 215-225 °C, and demold temperature 70-85 °C. Terminal products include 100-1,500 L agricultural sprayer tanks, seed-treatment mix vessels, molasses lick feeders, and farrowing crate floor inserts.
Where outdoor playground and street furniture components must retain impact strength at -20 °C and simultaneously meet toy-safety migration limits, Sclair MDPE 13J7 is processed under the requirements of EN 71-1:2014+A1:2018 for mechanical and physical properties, EN 71-3:2019 for migration of certain elements, and ASTM F1487-21 for public playground equipment in North America. The weathering requirement is validated by ISO 4892-2:2013, cycle 1, with impact retention measured after 5,000 h of artificial weathering. The formulation for this sector limits internally generated regrind to 15 wt% and uses 1.0-2.0 wt% heavy-metal-free colorant masterbatch; HALS-based UV stabilizer masterbatch is added at 2.0-4.0 wt% to preserve surface integrity and color. Double-wall rotomolded panels are run at a wall thickness of 5-8 mm; oven temperature is held at 265-290 °C, and a peak internal air temperature of 210-225 °C is maintained until mold-surface temperature uniformity is confirmed before forced-air cooling at 10-18 °C/min. Cooling fixtures are required for tunnel sections and slide shells to hold dimensional tolerance below ±1.5%. Terminal products include modular playground tunnels, slide beds, climbing wall panels, outdoor bench shells, and waste receptacle bodies.
Injection molded logistic components represent a secondary conversion route for Sclair MDPE 13J7 where the melt index of 7.0 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg allows filling of long flow paths without excessive clamp tonnage. The governing standards are ASTM D4976-12a for polyethylene molding and extrusion materials and, for food-contact articles, 21 CFR §177.1520 olefin polymer conditions; packaging components fall under EU heavy-metal limits in Directive 94/62/EC. The formulation contains 100 parts by weight of 13J7, 2-5 wt% injection-grade colorant masterbatch, and 0-10 wt% internally generated regrind; when food-contact compliance is required, regrind is restricted to internally generated material from the same approved formulation. Production uses a single-screw injection press with 20:1-24:1 L/D, melt temperature 190-230 °C, mold temperature 15-40 °C, injection pressure 50-90 MPa, and back pressure 0.5-1.5 MPa. Because the gate freezes rapidly in sections of 2.5 mm nominal wall at 30 °C mold temperature, the velocity-to-pressure switch must occur within 0.3-0.5 s, and pack/hold pressure is maintained at 40-60% of filling pressure for 6-12 s to compensate for volumetric shrinkage. Terminal products include intermediate bulk container frame components, collapsible crates, insulated fish tubs where the molder has completed 21 CFR §177.1520 compliance, and non-food closures.
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