| HS Code | 211145 |
| Material Type | Polypropylene Impact Copolymer |
| Density | 0.905 g/cm³ |
| Melt Flow Rate | 6 g/10 min at 230°C/2.16 kg |
| Tensile Modulus | 1200 MPa |
| Tensile Stress At Yield | 24 MPa |
| Tensile Strain At Yield | 9% |
| Flexural Modulus | 1150 MPa |
| Charpy Notched Impact Strength At 23 C | 45 kJ/m² |
| Vicat Softening Temperature | 145 °C |
| Heat Deflection Temperature At 0 45 Mpa | 85 °C |
As an accredited SABIC PP 5706P factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SABIC PP 5706P is packaged in 25 kg multilayer paper bags, palletized and stretch-wrapped for safe transport and storage. |
| Container Loading (20′ FCL) | SABIC PP 5706P packed in bags on pallets, loaded into 20′ FCL container, secured and ventilated for safe transport. |
| Shipping | SABIC PP 5706P is a polypropylene resin supplied as free-flowing pellets. It is non-hazardous and not regulated as dangerous goods for transport. Ship in clean, dry, moisture-proof packaging or containers, protected from direct heat and prolonged sunlight. Standard freight handling is safe; no special labeling required, though proper segregation from contaminants is advised. |
| Storage | Store SABIC PP 5706P in a clean, dry, well-ventilated area, away from direct sunlight, heat sources, and ignition sources. Keep packaging sealed to prevent moisture ingress and contamination. Maintain moderate temperatures below 40°C. Protect from UV exposure and mechanical damage. Avoid stacking excessively high to preserve pellet integrity and ensure first-in, first-out rotation. |
| Shelf Life | SABIC PP 5706P has a shelf life of at least one year when stored in original, dry, cool conditions away from sunlight. |
The specification of SABIC PP 5706P for PP-R hot and cold water pipe extrusion places a low-melt-flow random copolymer into the socket-fusion plumbing chain. The nominal melt flow rate of 0.60 g/10 min (ISO 1133-1, 230°C, 2.16 kg) and density of 0.900–0.910 g/cm³ (ISO 1183-1) provide high melt strength that stabilizes pipe wall concentricity during vacuum calibration of diameters from 16 mm to 125 mm. The resin is metered as a virgin stream at 96.0–98.5 wt%, with a stabilized color masterbatch at 1.0–2.0 wt%, a hindered phenol/phosphite antioxidant package at 0.10–0.30 phr, and calcium stearate acid scavenger at 0.05–0.10 phr; no mineral filler is introduced because filler reduces the thermal stability of socket fusion zones and shifts the hydrostatic failure mode from ductile to brittle. Compliance is anchored to ISO 15874-2:2013 clauses 5 to 8, ISO 9080:2012 long-term hydrostatic strength regression, DIN 8077:2008, NSF/ANSI/CAN 61, AS/NZS 4020, and EU 10/2011 for migration limits in potable contact. Pipe extrusion uses a grooved-feed single-screw extruder with a 30:1 L/D barrier screw, melt pump, and spiral mandrel die operated at a melt temperature of 190–220°C; vacuum calibration tanks maintain water at 10–30°C and line speed is controlled to hold wall thickness variation below ±0.1 mm. Pre-drying at 80°C for 2 h is required if storage relative humidity exceeds 60%; melt temperatures above 230°C accelerate stabilizer depletion and increase the risk of gel formation. Terminal products include SDR 7.4 PN 20 hot water pipe, SDR 11 PN 16 distribution pipe, SDR 13.6 PN 10 cold water pipe, socket fusion elbows, and distribution manifolds for residential and commercial plumbing networks.
Long-term hydrostatic strength in pressurized industrial effluent lines around SABIC PP 5706P is governed by the resin's resistance to slow crack growth and oxidative degradation at elevated temperature, not by its short-term burst pressure. In this sector the formulation ratio consists of 98.0–99.0 wt% base resin, 1.0–2.0 wt% carbon black masterbatch for UV screening, 0.20–0.40 phr hindered amine light stabilizer, 0.10–0.30 phr hindered phenolic antioxidant, and 0.05–0.10 phr calcium stearate; carbon black loadings above 2.5 wt% reduce elongation at break and lower the lower confidence limit of hydrostatic strength at 50 years. Pipe production uses a 33:1 L/D single-screw extruder with a grooved feed section, melt temperature of 200–230°C, and a water-cooled calibration sleeve; downstream butt fusion welding is carried out at 220–240°C with a bead-up pressure of 0.15 MPa and fusion pressure of 0.10 MPa. Compliance is referenced to ISO 15494:2015, ISO 9080:2012, and chemical resistance testing under ISO 175 for acids, alkalis, and salt solutions. Terminal products include acid and alkali drainage headers, plating shop effluent lines, brine transfer piping, and industrial water return lines. Service is not recommended for continuous contact with strong oxidizers or aromatic hydrocarbon streams, as these attack the amorphous phase and reduce the time to ductile-brittle transition under hoop stress.
| Sector | Standard designation | Test condition | Typical requirement |
|---|---|---|---|
| Potable water pipe | ISO 15874-2:2013 | Hydrostatic pressure at 70°C, 20 h | No leakage or rupture |
| Potable water system fitness | ISO 15874-5:2013 | Pressure cycling 1.5 MPa | No leakage at joint |
| Industrial effluent pipe | ISO 15494:2015 | Long-term hydrostatic regression | Design stress per material class |
| Chemical resistance | ISO 175 | Immersion in acid/alkali | Mass change within limit |
| Injection-moulded fitting | ISO 15874-3:2013 | Hydrostatic pressure at 70°C | No failure |
| Structured-wall drainage pipe | EN 13476-3 | Ring stiffness testing | Declared stiffness class |
Injection-moulded socket fusion fittings produced from SABIC PP 5706P must address a thicker-wall flow path than pipe extrusion, with a low melt flow rate of 0.60 g/10 min creating packing and weld-line challenges in multi-cavity tools. The formulation uses 100 parts PP 5706P, 0.05–0.10 phr sodium benzoate nucleating agent, 0.10–0.20 phr antioxidant package, and 1.0–2.0 wt% color masterbatch; impact modifiers are excluded because they reduce the long-term hydrostatic strength margin after socket fusion. Moulding is performed at a melt temperature of 210–230°C, a mould temperature of 20–50°C, and a hydraulic holding pressure of 40–70 MPa; gate diameter is set to at least 50% of the local wall thickness, and flow-length-to-wall-thickness ratio is held below 150:1 to prevent short shots. Weld lines are positioned away from the socket fusion entry plane to minimize hoop stress concentration during pressure cycling, and moulded fittings are annealed at 80–100°C for 2 h before hydrostatic testing to relax moulded-in orientation. Compliance is anchored to ISO 15874-3:2013, ISO 15874-5:2013, and ISO 1167 pressure testing. Terminal products include PN 20 socket fusion elbows, tees, reducers, couplings, and female threaded adapters for hot and cold water distribution networks.
Extruded sheet from SABIC PP 5706P is deployed where chemical containment liners must survive prolonged contact with acidic or alkaline process fluids without stress cracking. The formulation consists of 100 parts PP 5706P, 0.20–0.40 phr hindered phenolic antioxidant, 0.30–0.60 phr hindered amine light stabilizer, 0.05–0.10 phr calcium stearate, and 0.5–2.0 wt% pigment masterbatch. Sheet extrusion is performed on a single-screw extruder with a 33:1 L/D screw and flexible-lip sheet die feeding a three-roll calender; melt temperature is held at 200–230°C, roll temperatures at 60–85°C, and sheet thickness ranges from 2.0 mm to 10.0 mm. Fabrication uses hot-gas welding and extrusion welding at 220–260°C, with double-V weld geometries on sections above 5.0 mm to achieve joint efficiency above 90% of parent material. Compliance for chemical immersion is tested under ISO 175 and ASTM D543, with weld procedure qualification per DVS 2207-4. Terminal products include chemical storage tank liners, pickling bath liners, fume scrubber ducts, and laboratory drainage channels.
When corrugated drainage profiles push melt strength to its lower bound, the low melt flow rate of SABIC PP 5706P becomes the controlling process parameter rather than a limitation. Corrugated pipe is produced on a corrugator with vacuum forming and water spray cooling, using a melt temperature of 190–215°C and a die gap set to achieve a wall thickness of 0.8–1.5 mm. The formulation ratio is 100 parts PP 5706P, 2.0–2.5 wt% carbon black masterbatch for UV resistance, 0.10–0.30 phr antioxidant, and 0.10–0.30 phr processing aid. Compliance is referenced to EN 13476-3 and ISO 21138-3 for structured-wall PP piping. Terminal products include subsoil drainage pipes, cable protection conduits, and culvert liners. Published data for this specific configuration is limited, so corrugator speed and vacuum settings are established on line rather than transferred from solid-wall pipe data.
Glass-fibre reinforced PP flanges and pump housings derived from SABIC PP 5706P use the resin as the continuous matrix for short-glass-fibre compounds. The formulation contains 70.0–80.0 wt% PP 5706P, 20.0–30.0 wt% chopped glass fibre, 0.20–0.50 phr maleic anhydride grafted PP coupling agent, and 0.10–0.30 phr antioxidant package. Compounding is carried out on a 40:1 L/D co-rotating twin-screw extruder with side feeding of glass fibre downstream of the melting zone, melt temperature 210–230°C; the compound is then injection moulded at 220–250°C into flanges, pump volutes, and valve bodies. Mechanical acceptance is tested under ISO 527-2 and ISO 179-1/1eA Charpy notched impact at 23°C. Terminal products serve chemical transfer and water treatment circuits where metal replacement requires corrosion resistance and dimensional stability.
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For cast film and sheet extrusion operations that require a low-fog homopolymer with antistatic and anti-block functionality, SABIC PP 5706P is designated by SABIC as a polypropylene homopolymer grade with a melt mass-flow rate of 6.0 g/10 min under ISO 1133-1:2022 and a density of 0.905 g/cm³ under ISO 1183-1:2019. The grade contains no ethylene-propylene rubber phase; the property envelope therefore favors stiffness, thermal resistance, and surface hardness over impact toughness. This product is intended for cast film, flat-die sheet, and downstream thermoforming applications where optical clarity and dimensional stability at elevated temperature are required.
Extrusion of SABIC PP 5706P on a 75 mm single-screw line with a 30:1 L/D barrier screw and a 1.2 m slot die is typically performed at melt temperatures of 220°C to 260°C. Because the matrix is a high-crystallinity homopolymer, melt elasticity and die swell are lower than those of impact copolymer grades, which reduces edge neck-in at high draw ratios. Operation above 280°C accelerates oxidative chain scission, causing die-lip deposit formation and a measurable reduction in film dart impact; operation below 210°C raises melt viscosity and can produce sharkskin and transverse thickness variation. A water-cooled feed throat, compression ratio of 3:1 to 3.5:1, and screen pack filtration at 100 mesh are standard line configurations. The chill-roll temperature is maintained between 18°C and 25°C; lower settings increase quench-side crystallinity and haze, while higher settings can reduce roll-side gloss and promote blocking during rewind. Pellets stored at relative humidity above 60% should be dried at 80°C for 3 h with a desiccant dryer having a dew point of -30°C or lower to prevent splay from condensed moisture.
The melt mass-flow rate of 6.0 g/10 min under ISO 1133-1:2022 positions the grade for moderate-throughput cast film lines. The linear homopolymer structure exhibits shear thinning typical of broad molecular-weight-distribution polypropylene. Extrusion die pressure and motor load are lower than those of lower-MFR grades but higher than those of 12–15 g/10 min extrusion coating grades. This balance allows stable processing at line speeds of 50–120 m/min on cast film lines depending on die width and film thickness. The grade is not formulated for stretch-blow molding or for processes requiring strain-hardening melt strength.
The representative values in the following table are drawn from published product data for material selection and are not specification limits. Lot-to-lot variation is controlled by the manufacturer and should be verified against the release certificate for each batch.
| Property | Method | Value |
|---|---|---|
| Melt mass-flow rate, 230°C/2.16 kg | ISO 1133-1:2022 | 6.0 g/10 min |
| Density | ISO 1183-1:2019 | 0.905 g/cm³ |
| Tensile stress at yield | ISO 527-2:2012 | 34 MPa |
| Tensile elongation at yield | ISO 527-2:2012 | 10% |
| Flexural modulus | ISO 178:2019 | 1550 MPa |
| Notched Izod impact at 23°C | ISO 180/A:2019 | 3.0 kJ/m² |
| Vicat softening temperature A/50 | ISO 306:2013 | 154°C |
| Heat deflection temperature B/0.45 MPa | ISO 75-2:2013 | 94°C |
The combination of a 154°C Vicat A/50 and a 1550 MPa flexural modulus places the grade in the stiff, thermally resistant segment of the homopolymer film range. Published multi-axial impact data for this specific configuration is limited; notched Izod remains the standard discriminator under ISO 180/A.
For food-contact use, SABIC PP 5706P must be assessed against the current product safety datasheet. Olefin polymers fall under FDA 21 CFR 177.1520 and EU Regulation 10/2011, but specific migration limits for the antistatic and anti-block additives depend on the food simulant, contact time, and temperature. Under EU Regulation 10/2011, the overall migration limit for food-contact plastic materials is 10 mg/dm². Fatty food simulants can extract low-molecular-weight additives more aggressively than aqueous simulants; therefore, hot-filled or high-fat applications above 80°C require testing before conversion.
Random copolymer polypropylene incorporates ethylene into the chain, disrupting crystallinity and lowering the Vicat A/50 to approximately 125°C to 135°C under ISO 306. SABIC PP 5706P retains a Vicat A/50 of 154°C, which permits short-term contact with hot-fill temperatures that would deform random copolymer sheet. Compared with heterophasic impact copolymers, the homopolymer exhibits lower notched impact resistance at 23°C and a ductile-to-brittle transition near 0°C. Impact copolymer grades typically show notched Izod values above 25 kJ/m² at 23°C, whereas this grade is specified at approximately 3.0 kJ/m². The trade-off is a higher flexural modulus, which allows down-gauging in rigid packaging only when impact loading is not controlling. The comparison table below summarizes these class-level differences.
| Attribute | SABIC PP 5706P homopolymer | Random copolymer polypropylene | Heterophasic impact copolymer |
|---|---|---|---|
| Flexural modulus | 1550 MPa | 900–1100 MPa | 1100–1300 MPa |
| Notched Izod impact at 23°C | 3.0 kJ/m² | 6–10 kJ/m² | 25–60 kJ/m² |
| Vicat A/50 | 154°C | 125–135°C | 145–155°C |
| Typical low-temperature failure mode | Brittle near 0°C | Ductile to -20°C | High-energy ductile below -20°C |
Replacing amorphous sheet such as PET or PS with a semicrystalline homopolymer changes the heating profile and sag behavior. The sheet must be heated to a core temperature of 150°C to 165°C before forming; the temperature differential across the forming area should be controlled within ±5°C. PET and PS form after a sharp glass-transition-driven modulus drop, whereas PP 5706P softens over a broader interval and requires longer dwell time under the heater bank. On a pressure former with 250 kN clamp force, 5–6 bar forming pressure, and an aluminum mold temperature of 60°C, cycle times are longer than PS but shorter than impact PP at the same wall thickness. Mold release is influenced by surface roughness; polished surfaces with 0.8 μm Ra reduce ejection forces, while textured cavities require added draft of 1° to 3°. Mold shrinkage in both machine and transverse directions is typically 1.0% to 1.5% and stabilizes after approximately 48 h; parts should not be packed before this stabilization period if critical dimensions are specified.
Sheet produced from this grade is extruded at melt temperatures of 230°C to 250°C through a polishing three-roll stack. Roll temperatures are set between 40°C and 80°C depending on sheet thickness; sheet above 1.0 mm typically requires roll temperatures near 80°C to avoid warpage. Thermoforming at areal draw ratios above 3:1 can increase corner thinning beyond 40%, requiring positive assist or local plug temperature adjustment.
Operational boundaries for this grade follow from the homopolymer structure. Continuous service below 0°C with point impact is not recommended because of brittle failure; a heterophasic impact copolymer should be selected for freezer containers. The grade is not inherently UV-stabilized; outdoor service requires a UV masterbatch at 2–4 wt% or a carbon black loading tested under ISO 4892-2. Prolonged exposure to strong oxidizing acids at concentrations above 10% causes surface etching and molecular weight reduction. For printing and lamination, corona treatment to a surface tension of 38–42 mN/m is typical, but excessive treatment can oxidatively damage the surface and reduce heat-seal strength. The product is not formulated for high-melt-strength extrusion foam or blow molding processes; those applications require a strain-hardening polypropylene or a post-reactor modified grade. Recycled material from this grade can be incorporated only after verifying oxidative induction time against the virgin specification; repeated heat histories above 240°C deplete the stabilizer package and reduce long-term thermal stability.