| HS Code | 409655 |
| Density | 0.905 g/cm³ |
| Melt Flow Rate | 12 g/10 min (230°C, 2.16 kg) |
| Tensile Strength At Yield | 35 MPa |
| Flexural Modulus | 1500 MPa |
| Elongation At Break | 12% |
| Heat Deflection Temperature | 100 °C (0.45 MPa) |
| Vicat Softening Point | 155 °C |
| Izod Impact Strength Notched | 3.5 kJ/m² (23°C) |
| Rockwell Hardness | R-95 |
| Melting Point | 165 °C |
As an accredited Profax (Indelpro/Alpek) PP Homopolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Profax PP homopolymer is supplied in 25 kg bags, palletized and stretch-wrapped for safe transport and storage. |
| Container Loading (20′ FCL) | 20′ FCL loading of Profax PP homopolymer pellets in 25kg bags, palletized and securely stowed for safe, efficient transport. |
| Shipping | Profax (Indelpro/Alpek) PP Homopolymer ships as free-flowing pellets in bulk railcars, trucks, or 25 kg bags. Protect from moisture, heat, and contamination. Store in dry, ventilated areas away from oxidizers. Use clean equipment; avoid dust accumulation. Handle with proper PPE to prevent static ignition. |
| Storage | Store Profax PP homopolymer in a cool, dry, well-ventilated area away from direct sunlight, heat, open flames, and strong oxidizers. Keep containers tightly sealed to prevent moisture contamination and dust accumulation. Maintain moderate temperatures to avoid softening or degradation. Use proper grounding during handling and ensure storage area complies with local fire safety regulations. |
| Shelf Life | Profax PP homopolymer has an indefinite shelf life when stored in a cool, dry area away from direct sunlight and heat. |
High-fluidity Profax homopolymer grades in the 25 g/10 min to 40 g/10 min melt-flow band (ISO 1133-1:2022, 230 °C/2.16 kg) are processed on single-screw extruders with L/D 30:1 and barrier screw geometry delivering melt to spinnerets with 0.35 mm to 0.50 mm capillary diameter. Melt temperature is controlled at 225 °C to 245 °C. Quench air at 12 °C to 18 °C and 0.3 m/s to 0.8 m/s freezes filament surfaces before draw-jet attenuation at 0.4 MPa to 0.8 MPa. The resulting filaments reach 15 µm to 25 µm diameter and are deposited on a moving belt with basis weight from 10 g/m² to 50 g/m². Thermal bonding through heated calender rolls at 130 °C to 150 °C creates spunbond nonwovens for hygiene coverstock, medical barrier gown fabric, and filtration support layers.
The formulation for hygiene-grade spunbond requires additive discipline. Antioxidant package at 0.08 wt% to 0.15 wt% of a phenolic/phosphite blend and acid scavenger at 0.02 wt% to 0.06 wt% calcium stearate are melt-compounded on a 75 mm twin-screw extruder. Slip and antiblock concentrates are excluded because their migration to spinneret faces creates filament breaks at high draw speeds. Screen-changer pressure increase above 12 MPa at constant throughput indicates additive agglomeration or degraded gel accumulation.
Compliance for hygiene spunbond includes EU Regulation (EU) No 10/2011 overall migration limit 10 mg/dm², FDA 21 CFR 177.1520 for olefin polymers, and REACH Regulation (EC) No 1907/2006. Long-wear skin contact is assessed under ISO 10993-5:2009 and ISO 10993-10:2021 when the fabric is used in medical devices.
Core-layer polypropylene for biaxially oriented film must retain high isotacticity. Profax homopolymer grades with MFI 2.5 g/10 min to 4.0 g/10 min (ISO 1133-1:2022, 230 °C/2.16 kg) provide controlled crystallization and orientation strain hardening. Copolymer-rich core layers reduce tensile modulus and cause uneven transverse stretching at draw ratios above 7:1. The cast sheet is extruded through a 1.8 m slot die at 240 °C to 260 °C and quenched on a chill roll held at 30 °C to 40 °C. Reheat orientation is conducted at 140 °C to 160 °C for machine-direction stretching and 155 °C to 170 °C for transverse-direction stretching in a tenter oven. Line speed typically ranges from 300 m/min to 500 m/min. The orientation window is narrow: below 135 °C, microvoids form; above 170 °C, disorientation and thickness-profile deterioration occur.
Three-layer coex structures use a homopolymer core with no slip agent. The core contains 0.06 wt% to 0.12 wt% antioxidant and 0.02 wt% to 0.05 wt% acid scavenger. Skin layers receive antiblock masterbatch at 0.5 wt% to 2.0 wt% and slip concentrate at 0.3 wt% to 1.0 wt%, targeting a coefficient of friction below 0.30 measured under ASTM D1894-14.
Food-contact BOPP qualifies under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011. Specific migration of erucamide and other slip migrants must remain below 10 mg/kg in appropriate food simulants. Converted structures include metallized snack wrappers, clear overwrap, and pressure-sensitive label facestock after corona treatment at 42 mN/m to 46 mN/m.
Tape extrusion grades of Profax homopolymer with MFI 3.0 g/10 min to 4.5 g/10 min (ISO 1133-1:2022, 230 °C/2.16 kg) are extruded through flat dies with 0.8 mm to 1.2 mm die gap into a water quench bath at 30 °C to 40 °C. The quenched film is slit, then oriented in hot-air ovens at 110 °C to 140 °C. Draw ratio is set between 1:6 and 1:7. At draw ratios above 1:7, tape elongation at break declines below 12% (ISO 527-3:2018) and circular-loom breakage increases. Uncontrolled fibrillation appears at draw ratios near 1:8 when the molecular weight distribution is broad or when the water bath temperature varies by more than 5 °C.
The formulation for outdoor woven sacks includes hindered amine light stabilizer at 0.25 wt% to 0.50 wt%, calcium stearate at 0.05 wt% to 0.10 wt%, antioxidant at 0.08 wt% to 0.15 wt%, and pigment masterbatch at 2 wt% to 4 wt%. High pigment loadings alter quench rate and tape stiffness, requiring re-profiling of water bath and oven zones. End products include fertilizer sacks, pet-food bags, and FIBC bulk packaging.
FIBC fabrics are qualified under ISO 21898:2004 for non-dangerous goods packaging. UN dangerous-goods sacks require top-lift and cyclic drop tests as specified by the competent national authority. Food-contact woven sacks comply with FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011 when the homopolymer and masterbatch are food-grade.
On thin-wall packaging lines with clamp force between 1000 kN and 2500 kN, Profax homopolymer injection-moulding grades in the 12 g/10 min to 35 g/10 min range (ISO 1133-1:2022, 230 °C/2.16 kg) are processed at melt temperature 220 °C to 250 °C and mould temperature 20 °C to 45 °C. The reciprocating screw uses L/D 20:1 to 24:1 and compression ratio 2.5:1 to 3.0:1. Injection speed is set at 150 mm/s to 350 mm/s, with holding pressure at 60% to 80% of peak injection pressure. For caps and closures, nucleating agent at 0.10 wt% to 0.25 wt% raises the crystallization onset temperature from 108 °C to 126 °C measured by differential scanning calorimetry under ISO 11357-3:2018. Mould shrinkage ranges from 1.2% to 1.6% in flow direction and 1.4% to 1.8% transverse direction (ISO 294-4:2018). Warpage is observed when mould surface temperature gradients exceed 5 °C across the core or when hot-runner valve-gate timing varies by more than 0.3 s.
The packaging formulation uses antioxidant at 0.06 wt% to 0.12 wt%, acid scavenger at 0.03 wt% to 0.08 wt%, nucleating agent as above, and external lubricant at 0.05 wt% to 0.10 wt%. Colour concentrate is added at 1 wt% to 2 wt%. Amine-based antistatic additives are avoided because they can cause discolouration in high-temperature thin-wall moulding. For metal-detectable closures used in food processing, X-ray-detectable masterbatch is added at 1 wt% to 3 wt%; published data for this specific configuration is limited.
Food-contact dairy cups, deli containers, and closures are evaluated under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011. Overall migration must remain at or below 10 mg/dm² in food simulants.
| Application | Regulatory anchor | Test method or condition | Limit or criteria |
|---|---|---|---|
| Spunbond hygiene coverstock | EU Regulation (EU) No 10/2011; FDA 21 CFR 177.1520 | Overall migration | 10 mg/dm² |
| Spunbond medical barrier fabric | ISO 10993-5:2009; ISO 10993-10:2021 | Cytotoxicity; irritation | No cell toxicity; no irritation |
| BOPP food packaging | FDA 21 CFR 177.1520; EU Regulation (EU) No 10/2011 | Specific migration of slip additives | 10 mg/kg |
| Woven sacks and FIBC | ISO 21898:2004; FDA 21 CFR 177.1520 | Top-lift and drop test; food-contact migration | Pass UN or national authority requirements |
| Injection-moulded food contact | FDA 21 CFR 177.1520; EU Regulation (EU) No 10/2011 | Mould shrinkage via ISO 294-4:2018 | 10 mg/dm² overall migration |
| Thermoformed trays | FDA 21 CFR 177.1520; EU Regulation (EU) No 10/2011 | Food simulant overall migration | 10 mg/dm² |
| Extrusion-coated woven sacks | FDA 21 CFR 177.1520; EU Regulation (EU) No 10/2011 | Adhesion via ASTM F88/F88M-21 | Peel strength retained after filling |
Sheet extrusion for plug-assist thermoforming uses Profax homopolymer with MFI 1.0 g/10 min to 3.0 g/10 min (ISO 1133-1:2022, 230 °C/2.16 kg) at melt temperature 230 °C to 260 °C through a 900 mm to 1200 mm slot die with die land 0.2 mm to 0.8 mm. The three-roll stack is maintained at 60 °C to 90 °C. Roll temperatures below 55 °C quench the sheet surface too rapidly and induce differential shrinkage that appears as curl after trimming. Regrind addition above 30 wt% lowers extensional viscosity and creates sagging inside the plug-assist form station. Deep-draw depths above 50 mm require plug-timing accuracy of 0.1 s to avoid sidewall thinning below 45% of initial sheet thickness.
Food-grade sheet formulation includes nucleating agent at 0.05 wt% to 0.15 wt%, antioxidant at 0.06 wt% to 0.12 wt%, acid scavenger at 0.03 wt% to 0.08 wt%, and antistatic concentrate at 0.1 wt% to 0.3 wt%. Titanium dioxide masterbatch at 1 wt% to 4 wt% is used for white dairy cups. Thermoformed containers comply with FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011. End products include drink cups, produce trays, and bakery clamshells.
Gamma-irradiation at 25 kGy to 50 kGy changes the melt-flow response and oxidative stability of polypropylene homopolymer unless radiation-stable additive packages are selected. For syringe barrels and rigid diagnostic consumables, Profax homopolymer grades in the 18 g/10 min to 25 g/10 min MFI range (ISO 1133-1:2022, 230 °C/2.16 kg) are injection moulded on electric machines with clamp force 800 kN to 1600 kN inside ISO 14644-1:2015 Class 7 cleanrooms. Melt temperature is limited to 220 °C to 245 °C, and mould temperature is held at 15 °C to 30 °C. Hot-runner valve gates minimize gate vestige height below 0.1 mm, which is critical for syringe lubrication. Gamma doses above 50 kGy produce measurable yellowing and notch sensitivity.
The medical formulation excludes slip agents and animal-derived additives. Radiation-stable antioxidant package at 0.10 wt% to 0.20 wt%, acid scavenger at 0.02 wt% to 0.05 wt%, and optional radiolytic stabilizer at 0.05 wt% to 0.15 wt% are used. No phthalate plasticizers are present. Compliance anchors include USP 661.1 and USP 661.2 for plastic packaging systems, ISO 10993-5:2009 for cytotoxicity, ISO 10993-10:2021 for irritation and skin sensitization, and FDA 21 CFR 177.1520 for food-contact drug-delivery accessories where applicable. End products include syringe barrels, pipette tips, and specimen containers.
| Process | MFI range | Melt temperature | Critical processing boundary | Reference method |
|---|---|---|---|---|
| Spunbond nonwoven | 25–40 g/10 min | 225–245 °C | Screen-changer pressure 12 MPa max | ISO 1133-1:2022 |
| BOPP film core | 2.5–4.0 g/10 min | 240–260 °C | MD 4.5:1–5.5:1; TD 7:1–9:1 | ISO 1133-1:2022 |
| Raffia tape | 3.0–4.5 g/10 min | 220–250 °C | Draw ratio 1:6–1:7 | ISO 527-3:2018 |
| Thin-wall injection moulding | 12–35 g/10 min | 220–250 °C | Mould temperature gradient 5 °C max | ISO 294-4:2018 |
| Thermoformed sheet | 1.0–3.0 g/10 min | 230–260 °C | Regrind 30 wt% max | ISO 1133-1:2022 |
| Medical injection moulding | 18–25 g/10 min | 220–245 °C | Gamma dose 25–50 kGy | ISO 10993-5:2009 |
| Extrusion coating | 12–25 g/10 min | 260–290 °C | Substrate dyne level 40–46 mN/m | ASTM F88/F88M-21 |
In extrusion coating, the melt curtain is generated from Profax homopolymer coating grades with MFI 12 g/10 min to 25 g/10 min (ISO 1133-1:2022, 230 °C/2.16 kg) at melt temperature 260 °C to 290 °C. The slot die gap is 0.4 mm to 0.8 mm, and the air gap between die exit and laminating nip is 150 mm to 250 mm. Coating thickness is controlled from 15 µm to 30 µm. Adhesion to the fabric surface depends on corona pre-treatment at 40 mN/m to 46 mN/m measured with dyne solutions. Without corona treatment or without a preheated substrate at 60 °C to 80 °C, peel strength falls below 5 N/15 mm (ASTM F88/F88M-21) and the coating delaminates during sack filling.
The coating formulation includes antioxidant at 0.06 wt% to 0.12 wt% and acid scavenger at 0.03 wt% to 0.08 wt%. For untreated fabric or moisture-barrier service, 2 wt% to 5 wt% of maleic anhydride-grafted polypropylene tie resin is blended into the coating to promote adhesion. Extrusion-coated woven sacks for fertilizer, pet food, and industrial powders are tested under ISO 21898:2004. Food-contact grades comply with FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011 for dry-food packaging.
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Profax (Indelpro/Alpek) PP Homopolymer is a semicrystalline isotactic polypropylene resin produced without intentional ethylene-derived comonomer sequences. The material meets the generic designation PP-H under ISO 1873-1 and is characterized by a solid-state density of 0.900–0.910 g/cm³ at 23°C according to ISO 1183-1:2019 and a melting peak from 160°C to 165°C by differential scanning calorimetry under ISO 11357-3:2018 at 10 K/min. Profax homopolymer grades are sold with a four-digit suffix that identifies the conversion route and nominal melt-flow range. Representative published datasheets for the Profax 6331 injection-molding grade list a nominal melt flow rate of 12 g/10 min at 230°C/2.16 kg using ISO 1133-1:2022, and Profax 6329 is assigned to lower-flow extrusion applications. The absence of an ethylene-propylene rubber phase produces a hard, stiff matrix with a narrow processing window for impact modification and a higher melting point than random copolymers.
Melt flow rate depends on weight-average molar mass, molar mass distribution breadth, and controlled-rheology peroxide adjustment. For Profax homopolymer grades, injection-moulding variants are typically supplied in the range 8–100 g/10 min, while raffia, tape, and sheet extrusion grades are constrained between 2.0 g/10 min and 3.5 g/10 min. The apparent shear viscosity at 230°C and 100 s⁻¹ moves inversely with melt flow rate; high-flow injection grades reduce cavity pressure loss in thin-wall tools, whereas low-flow extrusion grades retain melt strength for tape-line bubble stability. Single-point MFR data do not resolve shear-sensitivity or extensional-viscosity differences, so ISO 11443:2021 capillary rheometry is required for lot-to-lot viscosity comparison when changing between Profax homopolymer grades or between suppliers.
The weight-average molar mass of extrusion grades is typically between 250,000 g/mol and 450,000 g/mol, while high-flow injection grades can be below 180,000 g/mol depending on peroxide-controlled visbreaking. Polydispersity index after controlled rheology is commonly 3.5–6.0 by high-temperature gel permeation chromatography under ISO 16014-4:2019, but published Profax grade-specific molar mass data are limited because suppliers often control melt-flow and rheological fingerprints rather than absolute molar mass.
| Conversion route | Typical melt flow rate | Critical processing parameter | Reference method |
|---|---|---|---|
| Injection molding | 8–100 g/10 min | Peak cavity pressure below 70 MPa for thin-wall tools | ISO 1133-1:2022 |
| Raffia/tape extrusion | 2.0–3.5 g/10 min | Melt strength at die exit; quench bath gap 3–6 mm | ISO 11443:2021 |
| Cast film/sheet | 2.5–8 g/10 min | Chill-roll temperature 15–30°C for haze control | ISO 1133-1:2022 |
| Spunbond/staple fiber | 12–40 g/10 min | Spinneret pressure drop and melt blowing | ISO 11443:2021 |
On injection-moulding lines, Profax homopolymer grades are processed with a barrel temperature profile from 200°C to 250°C, a nozzle set-point of 230°C to 250°C, and a mould temperature of 20°C to 60°C. The hydraulic injection pressure required for a thin-wall container with a flow length/wall thickness ratio above 150:1 can push peak cavity pressure above 50 MPa; tools should therefore be sized with a clamp force envelope that accounts for projected area and melt pressure at transfer. In extrusion, a twin-screw line with L/D 36–40 and a strand or underwater pelletizer is used for compounding, but direct end-use extrusion of Profax homopolymer sheet and tape typically employs single-screw machines with barrier screws and screen packs of 100–250 µm to remove oxidative gel. Published data for very high melt-flow Profax homopolymer grades above 80 g/10 min in melt-blown nonwoven lines is limited; capillary rheometry and spinneret pack-pressure data should be collected before commercial trials.
Cast-film and biaxially oriented polypropylene lines using Profax homopolymer require control of water-bath or chill-roll temperature and stretch ratios. The homopolymer’s high crystallization rate under quench conditions at 15–30°C can produce haze if roll-contact is uneven, so air-knife pressure and roll temperature uniformity are monitored. In tenter-frame BOPP, sequential stretching at machine-direction ratio 4.5–5.5:1 and transverse-direction ratio 7–10:1 is common for homopolymer films, but the upper limit depends on molecular weight distribution. In spunbond fiber lines, the absence of ethylene comonomer gives fast solidification and high fiber tenacity; however, line speeds above 3000 m/min require tight grade-controlled MFR because low-melt-strength resin can cause whipping instability between the die and the take-up screen.
Polypropylene homopolymer undergoes chain scission when melt temperature and residence time combine beyond the stabilizer package’s protection threshold. Profax homopolymer grades are normally supplied with a phenolic/phosphite antioxidant system that protects against oxidative degradation at melt temperatures up to 250°C for short cycles, but automatic screw-holding or hot-runner dwell times exceeding 15 min can increase yellowness index and lower melt viscosity. The recommended melt temperature range for most Profax homopolymer conversion operations is 210–250°C; above 260°C, processing residuals and peroxide decomposition products can produce aldehydes and ketones that surface as plate-out on vacuum vents. Pre-drying is not required when pellets are sourced in sealed, moisture-protected packaging. If storage relative humidity exceeds 60% or condensation is visible, a desiccant dryer at 80°C for 2–3 h is sufficient to restore surface moisture below 0.05 wt% before processing.
On production twin-screw extruders, dead spots in adapter sections and screen changers are common sites for thermomechanical degradation. Melt-temperature probes should be located after the breaker plate, not only in the die, because localized viscous heating can produce temperature spikes of 10–15°C above the barrel set-point. Frequent vent-port fouling indicates excessive volatile load or insufficient stabilizer, not normal operation. Purging with a high-viscosity polypropylene purge compound after each shutdown or before long hold periods reduces cross-linked gel and black specks in subsequent sheet and film runs.
Compared with heterophasic impact copolymers, Profax homopolymer exhibits higher stiffness and lower low-temperature impact resistance. A representative injection-molding homopolymer grade tested under ISO 527-2:2012 gives a tensile yield stress of 30–40 MPa and a flexural modulus under ISO 178:2019 of 1200–1600 MPa. The comparable heterophasic impact copolymer often gives a flexural modulus below 1100 MPa but a notched Charpy impact at −20°C above 6 kJ/m², whereas the homopolymer typically falls below 3 kJ/m² under ISO 179-1:2020. Homopolymer also shows higher crystallinity-induced mold shrinkage, commonly 1.0–2.0% in flow and transverse directions with ISO 294-4:2018 test plaques, so tool dimensions must be compensated differently than for impact-copolymer or random-copolymer grades.
Direct comparison with ASTM data requires attention to specimen geometry and test speed. ASTM D638-14 Type I bars and ASTM D790-17 Method I are not directly interchangeable with ISO 527-2:2012 and ISO 178:2019 values; the difference in support span, specimen thickness, and strain rate can shift reported flexural modulus by 5–10%.
Specific Profax homopolymer grades intended for food-contact packaging can be formulated to comply with FDA 21 CFR 177.1520 olefin polymer requirements and the overall migration limits of EU Regulation No 10/2011, provided that the finished article is evaluated for the intended food type and contact duration. Electrical and electronic applications may require verification against RoHS Directive 2011/65/EU and REACH Regulation 1907/2006 candidate-list restrictions. Medical packaging grades may require additional testing under ISO 10993-1:2018 and pharmacopoeial monographs such as European Pharmacopoeia 3.1.3.
| Application domain | Primary standard | Verification condition |
|---|---|---|
| Food contact | FDA 21 CFR 177.1520 | Finished-article migration testing required |
| EU food contact | Regulation 10/2011 | Overall migration by EN 1186-1:2002 |
| Toys/consumer articles | EN 71-3 | Extraction limits by material category |
| Electrical/electronic | RoHS 2011/65/EU | Exemptions apply by application |
In thin-wall packaging, the selection difference is driven by the trade-off between stiffness, drop impact, and processing pressure. Profax homopolymer provides the higher elastic modulus needed for wall-thickness reduction, but it may fail brittlely at sub-ambient temperatures when a filled package is dropped. Heterophasic impact copolymers absorb more energy through rubber-phase cavitation and exhibit lower flexural modulus. The homopolymer’s narrow sealing window is also a limitation in multilayer lamination; its melting peak of 160–165°C requires seal-bar temperatures above 170°C, while random copolymers with ethylene sequences seal below 150°C. In extrusion coating and BOPP film, however, the homopolymer’s higher crystallinity and lower extractable rubber fraction produce better stiffness and optics than impact-copolymer films, provided that the lower hot-tack strength is acceptable.