Products

Arya Sasol MDPE 3313

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    Specifications
    HS Code 776634
    Product Name Arya Sasol MDPE 3313
    Polymer Type Medium Density Polyethylene
    Density 0.933 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.25 g/10 min
    Melting Point 125 °C
    Vicat Softening Point 115 °C
    Tensile Strength At Yield 17 MPa
    Tensile Strength At Break 28 MPa
    Elongation At Break >600%
    Flexural Modulus 800 MPa
    Environmental Stress Crack Resistance >1000 h
    Hardness 60 Shore D
    Impact Strength Charpy Notched 20 kJ/m²
    Brittleness Temperature < -70 °C
    Water Absorption < 0.01%
    Thermal Conductivity 0.35 W/m·K
    Dielectric Constant 2.3
    Volume Resistivity >10^16 Ω·cm

    As an accredited Arya Sasol MDPE 3313 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Arya Sasol MDPE 3313 is supplied in 25 kg polypropylene woven bags, palletized for industrial handling and storage.
    Container Loading (20′ FCL) Arya Sasol MDPE 3313 is packed in 25 kg bags and loaded into a 20-foot FCL container, secured for export shipment.
    Shipping Arya Sasol MDPE 3313 is shipped as a non-hazardous polyethylene resin, typically in 25 kg bags or jumbo bags, palletized and stretch-wrapped. Use dry, ventilated containers under HS code 3901.90; protect from moisture, heat, and direct sunlight. No special dangerous-goods labeling is required.
    Storage Store Arya Sasol MDPE 3313 in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizers. Keep packages closed, palletized, and off the floor to prevent moisture and contamination. Avoid prolonged UV exposure and handle bags carefully to prevent tearing. Maintain good housekeeping and stock rotation, using first-in, first-out. Store separately from incompatible materials.
    Shelf Life Typically 12 months from production when stored in original unopened packaging, protected from direct sunlight, heat, moisture, and contamination.
    Application of Arya Sasol MDPE 3313

    For buried potable water service laterals and distribution mains, Arya Sasol MDPE 3313 is processed into solid-wall pipe on a single-screw extruder with grooved feed bushing, barrier screw geometry, and a screw L/D ratio of 30:1 to 37:1. The resin falls within the medium-density class, with density between 0.930 g/cm³ and 0.940 g/cm³ under ISO 1183-1, which provides lower crystallinity and improved stress relaxation during slow crack growth loading. Barrel temperatures before the adapter are typically set from 180°C to 220°C, while adapter and die zones are held at 200°C to 230°C to keep melt temperature inside the pipe extrusion window without exceeding 235°C, above which oxidation initiates and wall surface gloss becomes non-uniform. A feed-throat temperature below 70°C is maintained; when the throat is heated above 65°C with carbon black masterbatch or recycled flake present, hopper bridging occurs and the resulting screw starvation appears as periodic longitudinal wall-thickness oscillation. The compound is blended with carbon black masterbatch to a final loading of 2.0% to 2.5% by weight where outdoor exposure is specified, and dispersion is checked according to ISO 18553 for particles or agglomerates larger than 63 µm. Pipe classification under ISO 12162 places the material in the PE80 category if the minimum required strength from long-term hydrostatic regression is 8.0 MPa at 20°C; with a service coefficient C of 1.25 under ISO 4427-1, the allowable pressure ratings for PE80 solid-wall pipe are PN 12.5 for SDR 11, PN 10 for SDR 13.6, PN 8 for SDR 17, and PN 6 for SDR 21. The upper service temperature for pressure-rated operation is 40°C; continuous exposure above that threshold requires derating and confirmation because strength decreases with temperature along the ISO 9080 regression line. Potable water certification is not resin-inherent; finished pipes must be tested under local schemes such as AS/NZS 4020, NSF/ANSI/CAN 61, or EN 1622 depending on the market. Terminal products include blue municipal service laterals, black distribution mains, and rural water transfer lines with outside diameters from 20 mm to 630 mm. Published datasheet values for this specific grade should be verified on the supplier certificate of analysis before locking extrusion setpoints. Installation constraints include avoidance of prolonged contact with high chlorine dioxide residuals or hydrocarbon-contaminated backfill exceeding the limits specified in EN 12201-1, because localized oxidative chain scission can accelerate brittle crack initiation at the inner wall surface.

    SDRPN for PE80 at C=1.25Maximum Operating Pressure at 20°C
    SDR 11PN 12.51.25 MPa
    SDR 13.6PN 101.00 MPa
    SDR 17PN 80.80 MPa
    SDR 21PN 60.60 MPa
    SDR 26PN 50.50 MPa

    What Limits Rapid Crack Propagation in Buried Gas Distribution Laterals?

    Rapid crack propagation in pressurized gas distribution pipe is governed by the critical temperature and critical pressure measured on notched pipe under ISO 13477; PE80 MDPE formulations such as Arya Sasol MDPE 3313 are used where ductile failure must dominate at minimum service temperatures encountered in buried gas networks. Gas lateral extrusion typically uses a black compound with 2.0% to 2.5% carbon black by weight, and the final pipe is often rated for natural gas service up to 0.4 MPa at 20°C for SDR 11 construction based on ISO 4437, EN 1555-2, and AS/NZS 4130 design rules. During extrusion, melt temperature is held at 200°C to 220°C, and vacuum calibration uses closed-loop diameter control because out-of-roundness above 1% reduces butt fusion contact area and creates leak paths. Butt fusion joining follows DVS 2207-1; the heater plate surface temperature is set between 200°C and 220°C, the fusion bead-up pressure is 0.15 MPa to 0.17 MPa interfacial pressure, and the cooling time under joining pressure is extended beyond 8 min for wall thickness above 20 mm. A common field failure occurs when the plate temperature dips below 195°C or when the pipe ends are not re-machined after exposure to wind-borne dust, producing a cold-fusion joint that passes visual bead inspection but fails hydrostatic testing. The lower crystallinity of MDPE relative to HDPE reduces the tendency for rapid crack propagation and improves slow crack growth resistance under rock impingement. Terminal products include buried gas service laterals, distribution mains, and gas collection lines where coiled lengths up to 160 mm diameter reduce fusion joint counts. The upper service temperature for gas pressure rating is capped at 40°C by ISO 4437; operation above that limit requires pressure derating and utility approval.

    Thin-wall micro-irrigation laterals are extruded from MDPE 3313 on high-speed tubing lines where the melt passes through a screen pack of 60/120 mesh to remove gel particles and carbon black agglomerates that would otherwise accumulate at the die lip and create longitudinal score lines in walls as thin as 0.3 mm. The extrusion window for continuous lateral production with wall thickness between 0.3 mm and 0.8 mm requires melt temperatures of 190°C to 220°C and vacuum calibration with closed-loop laser diameter control; excursions below 185°C induce sharkskin melt fracture at high line speed, while excursions above 230°C cause sagging in the air gap and wall eccentricity. Cooling water temperature is maintained at 20°C to 35°C because lower temperatures freeze the outer surface before the inner wall has shrunk onto the calibrator sleeve, producing reversed ovality after release. Formulation includes 2.0% to 2.5% carbon black for UV stabilization, and the finished tubing is tested for hydrostatic pressure resistance under ISO 1167-1 or bursting and dimensional performance under ISO 9261 as applicable for agricultural emitters. The MDPE matrix resists stress cracking at emitter barb insertion points, where local strain concentration around barbs is the main failure origin in rigid HDPE grades. Terminal products include pressure-compensating dripperlines, non-pressure-compensating emitter laterals, and subsurface drip tape for row crops. When relative humidity exceeds 85%, surface moisture should be removed before extrusion, because vapor entrapment in the melt generates pinholes in walls thinner than 0.5 mm and can produce random pressure losses during field testing.

    Flat-Die Geomembrane Sheet and Dual-Track Wedge Welding Windows

    Geomembrane lining panels made from MDPE 3313 are produced on flat-die sheet lines with polished three-roll cooling stacks, with thickness from 1.0 mm to 2.5 mm and net widths up to 8,000 mm. Flat-die extrusion uses a melt temperature of 190°C to 215°C, and the roll gap is adjusted to control thickness variation within ±5% because wedge welding speed and final seam peel strength are sensitive to panel thickness mismatch. The lower density of MDPE compared with HDPE reduces bending stiffness and eases deployment in cold weather, but it also requires that panel rolls be stored on pallets to prevent flattening and stress whitening. Dual-track hot wedge welding is the dominant joining method; wedge temperature is raised until the seam shear elongation and peel strength satisfy project specifications, typically starting at 260°C and adjusted upward in 10°C increments as ambient temperature and wind speed change. Seam integrity is verified by air channel pressure testing according to ASTM D5820, and the bonded seam is rejected if pressure loss exceeds the specified limit. The material’s oxidative induction time should be checked under ASTM D3895 or EN 728 to confirm adequate antioxidant retention before installation, and the panel surface must be cleaned of dust, moisture, and oxide films before welding because contamination lowers peel strength below the minimum specified for the project. Terminal products include landfill caps, temporary pond liners, secondary containment basins, and canal lining panels where moderate chemical resistance and lower flexural modulus are specified.

    When the Top Coat in Three-Layer Steel Pipe Coating Must Withstand Cathodic Disbondment

    Three-layer external coating systems specified under ISO 21809-1 for welded steel transmission pipe comprise a fusion-bonded epoxy primer, an adhesive tie layer, and a polyolefin top coat. MDPE 3313 is applied as the top coat through a side-extrusion flat die at 200°C to 230°C onto the rotating pipe, with layer thickness controlled between 1.8 mm and 3.5 mm. The top coat’s slow crack growth resistance and low water permeability are evaluated in long-term cathodic disbondment testing at 1.5 V applied potential and 65°C surface temperature for 28 days; disbondment radius and adhesion retention are pass/fail criteria defined by ISO 21809-1. The extruder output is matched to pipe rotation speed and line speed to prevent melt overheating at the die lips, and the substrate must be preheated to the tie-layer manufacturer’s specified range before top coat application. If the top coat melt temperature exceeds 235°C, the adhesive tie layer can over-soften and lose interfacial adhesion to the epoxy primer; if the melt temperature falls below 195°C, the top coat does not wet the tie layer sufficiently and holiday testing under ASTM D5162 may reveal pinholes. Terminal products include oil, gas, and water transmission pipelines requiring mechanical protection during horizontal directional drilling, rocky backfill, and river crossings.

    Corrugated and ribbed underground conduit is manufactured from MDPE 3313 on corrugator lines with continuously oscillating forming blocks, where the pipe geometry alternates between crest and valley wall sections to achieve high ring stiffness at reduced material mass. Melt temperature is kept at 190°C to 220°C, and corrugator block temperature is maintained between 40°C and 70°C to prevent track marking and stress cracking on the crest walls. The product is tested for crush resistance and impact at 23°C and at low temperature in accordance with IEC 61386 or UL 651A. The MDPE matrix provides a balance of stiffness, coilability, and slow crack growth resistance for diameters up to 160 mm. Extrusion output must be coordinated with corrugator block speed; melt temperature above 230°C causes wall thinning at the crests and a collapse of the corrugated geometry, while melt temperature below 185°C raises melt pressure, reduces throughput, and can freeze the valley sections during block closure. Terminal products include fiber optic raceways, buried telecom ducts, and cable protective conduit where corrugated wall profiles permit high load-bearing capacity with lower resin consumption than solid-wall counterparts.

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