| HS Code | 415776 |
| Melt Flow Rate | 40 g/10 min |
| Density | 0.90 g/cm³ |
| Tensile Yield Strength | 35 MPa |
| Elongation At Break | 12% |
| Flexural Modulus | 1450 MPa |
| Notched Izod Impact Strength | 2.5 kJ/m² |
| Heat Deflection Temperature | 100 °C |
| Vicat Softening Temperature | 152 °C |
| Rockwell Hardness | 95 R |
| Mold Shrinkage | 1.5% |
| Ash Content | 0.03% |
| Isotactic Index | 96% |
As an accredited Oriental Energy S2040,PPH Fiber / Spinning factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Oriental Energy S2040 PPH Fiber/Spinning is packed in 25 kg polyethylene-lined woven bags, palletized for shipment. |
| Container Loading (20′ FCL) | Container loading: 20′ FCL loaded with Oriental Energy S2040 PPH Fiber/Spinning in 25 kg bags, palletized and shrink-wrapped for export. |
| Shipping | Oriental Energy S2040, PPH Fiber/Spinning is shipped as a non-hazardous polypropylene homopolymer resin, typically packed in 25 kg bags or jumbo bags. It should be transported in dry, covered containers at ambient temperature, protected from moisture, direct sunlight, and contamination. Not regulated as dangerous goods for transport. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers/packages closed and palletized to prevent moisture, dust, and contamination. Protect from weather and UV exposure. Avoid static buildup and follow SDS/local regulations. Use first-in, first-out, and keep away from incompatible materials. Do not store near food, drink, or animal feed. |
| Shelf Life | Typical shelf life is 24 months when stored in original unopened packaging, dry, away from direct sunlight, and below 40°C. |
Oriental Energy S2040 is classified as a polypropylene homopolymer fibre/spinning grade with a reported nominal melt flow rate of 36 g/10 min measured under ISO 1133-1:2022, 230°C/2.16 kg. The material is limited to downstream routes requiring melt spinning, spinline drawing, and fibre orientation. It is not intended for meltblown microfibre production where melt flow rates above 100 g/10 min are commonly required; published data for that specific configuration is limited. The scenarios below are restricted to industrial conversion routes in which S2040 is used as the dominant polymer phase or as the matrix fibre in nonwoven and fibre-reinforced products. Each scenario includes the applicable compliance framework, addition ratio, production equipment configuration, and terminal product categories.
Spunbond nonwoven conversion of S2040 has been characterized on single-beam and multi-beam Reifenhäuser Reicofil-type lines with working widths from 1.6 m to 4.2 m and positive-displacement spin pumps of 5–10 cm³/rev. The melt temperature at the die is maintained at 220–245°C, while extruder barrel zones are ramped from 180°C at the feed throat to 230°C at the metering section. Quench air at 10–18°C stabilizes filament attenuation before suction drawing, and calender bonding is performed with steel-rubber roll pairs at 145–160°C with nip pressure adjusted to target basis weight. Industry compliance for hygiene and medical spunbond includes FDA 21 CFR §177.1520 for polypropylene homopolymer as an olefin polymer in food-contact applications, EU Regulation 10/2011 with an overall migration limit of 10 mg/dm² for dry and aqueous food simulants, and ISO 10993-5:2009 plus ISO 10993-10:2013 for medical device materials requiring cytotoxicity and skin irritation evaluation. Medical barrier fabric claims are additionally assessed under EN 13795-1:2019 for microbial penetration and linting performance classes.
Dosing in spunbond formulations uses S2040 at 100 phr as the matrix; process aid masterbatch is introduced through gravimetric feeders at 0.5–2.0 wt%, and colour or TiO₂ masterbatch at 2.0–4.0 wt% with a PP homopolymer carrier of comparable melt flow rate. Spin finish is applied by kiss roller at 0.15–0.40 wt% on fibre mass to reduce electrostatic build-up without over-finishing calender roll surfaces. Process conflicts on high-speed lines are observed when die temperature exceeds 245°C, leading to oxidative degradation and increased spin pack pressure; when TiO₂ masterbatch exceeds 4.0 wt%, die-hole plugging and filament breaking may increase. Terminal product types include hygiene backsheet, surgical gown fabric, face mask outer layers, crop cover, furniture wrap, and spunbond geotextile separator fabric.
Fibre-reinforced concrete and needlepunched geotextile markets consume S2040 in staple fibre form because rapid melt filtration and controlled fibre-diameter distribution reduce carding stoppages and fibre balling. In concrete, EN 14889-2:2006 governs geometry- and alkali-resistance requirements for polymer fibres, while ASTM C1116/C1116M-23 classifies synthetic fibres as Type III reinforcement for crack control. Geotextile compliance includes ISO 9863-1:2016 for thickness under specified pressure, ISO 11058:2019 for water permeability perpendicular to the plane, and ASTM D5035-11(2019) for breaking force of textile fabrics. For outdoor durability, EN 12224:2000 is cited as the weathering resistance method. Staple fibre addition ratios for concrete are 0.6–1.8 kg/m³, equivalent to 0.1–0.3 vol%, which limits plastic shrinkage crack width without severe workability loss. Geotextile fibre formulations use S2040 at 100 phr, carbon black masterbatch at 2.0–3.0 wt%, and spin finish at 0.30–0.60 wt% based on fibre mass. Downstream production combines extrusion through multi-hole spinnerets, water quench at 20–35°C, drawing at 3.0–5.0 ratio, crimping, and cutting to 38–75 mm for carded needlepunch webs or 6–12 mm for concrete micro-reinforcement. The drawn staple is carded, cross-lapped, and needlepunched at 120–200 punches/cm² to form geotextile fabrics from 150 g/m² to 800 g/m². Terminal finished products include polypropylene geotextile separation layers, drainage composites, erosion-control blankets, fibre-reinforced concrete floor slabs, shotcrete tunnel linings, and precast concrete elements.
Continuous multifilament yarn lines running S2040 require strict draw-ratio control because residual torque after twisting is influenced by spinline cooling rate and draw ratio. Compliance standards for textile and rope products include ASTM D2256-10(2015) for tensile properties of yarns by single-strand method, ISO 2307:2019 for rope physical properties, and EN ISO 1968 for fibre rope terms and definitions. When used in food-contact agricultural netting, FDA 21 CFR §177.1520 applies. The formulation addition ratio starts from 100 phr S2040; UV-stabilized products incorporate hindered amine light stabilizer masterbatch at 1.0–3.0 wt%, processing stabilizer at 0.10–0.30 wt%, and spin finish at 0.40–0.80 wt%. Downstream production uses spinneret hole counts from 60 to 120 per yarn end, water-bath or air quench at 20–40°C, two-stage drawing with a total draw ratio of 5.0–7.0, and heated godets at 120–140°C to set molecular orientation. Terminal finished product types include low-to-medium tenacity industrial sewing thread, agricultural twine, safety netting, marine netting, geogrid yarn, and cable filler. High-tenacity heavy rope output is not preferred because the melt flow rate of S2040 is higher than the 4–10 g/10 min range typical for low-MFR rope grades; published data for high-tenacity conversion of S2040 is limited.
In monofilament extrusion lines equipped with 30:1 L/D single-screw extruders and water-bath quench tanks, S2040 is constrained to circular cross-sections above 0.15 mm diameter because the reported nominal melt flow rate of 36 g/10 min lowers melt strength at higher draw ratios. Compliance standards for industrial polyolefin monofilament include ASTM D3218 for polyolefin monofilament, EN ISO 2062 for yarn tensile testing, and REACH Annex XVII restrictions applicable to certain substances. Food-contact conveyor belts or nets made from S2040 monofilament require FDA 21 CFR §177.1520 and EU Regulation 10/2011 migration compliance. Formulation addition ratios use S2040 at 100 phr, UV masterbatch at 2.0–5.0 wt%, and slip/processing package at 0.5–1.0 wt%. If low surface friction is required, external lubricant is applied at 0.2–0.5 wt% by dip bath. Downstream production involves extrusion through a flat die or monofilament spinneret, quenching in water at 25–45°C, orientation in a hot-air oven at 120–150°C with draw ratio 6.0–9.0, and relaxation of 5–8% in a second oven to control shrinkage. Terminal finished products include brush bristles, industrial netting, zipper monofilament, spiral conveyor belting, and sieving fabric.
Carded staple webs containing S2040 are exposed to through-air oven temperatures between 135°C and 145°C when blended with low-melting sheath-core bicomponent binder fibre; the process avoids melting the S2040 homopolymer phase, whose peak melting temperature is 160–165°C when measured by differential scanning calorimetry under ISO 11357-3:2018. Compliance standards for automotive interior trim include FMVSS 302 for horizontal burn rate, ISO 3795:2019 for road vehicle flammability, and DIN 75201 for fogging behaviour. Acoustic insulation may be tested under ISO 10534-2:1998 for sound absorption coefficient. The addition ratio for S2040 staple ranges from 80–90 wt%, with 10–20 wt% bicomponent PP/PE binder fibre; siliconized finish is applied at 0.20–0.40 wt% to improve re-openability after carding. Downstream production begins with bale opening, carding, cross-lapping, and through-air bonding at 135–145°C with air velocity of 1.0–2.0 m/s. The bonded web is cooled to below 50°C before edge trimming and roll winding. Terminal finished products include automotive headliner felt, door panel absorber pads, trunk liner, seat-back felt, and under-bonnet insulation covers.
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