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SABIC PP Homopolymer 578P

    • Product Name: SABIC PP Homopolymer 578P
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 111863
    Melt Flow Rate 230 C 2 16 Kg 47 g/10 min
    Density 0.905 g/cm3
    Tensile Stress At Yield 36 MPa
    Elongation At Yield 10 %
    Flexural Modulus 1650 MPa
    Charpy Notched Impact Strength 23 C 2.0 kJ/m2
    Izod Notched Impact Strength 23 C 2.0 kJ/m2
    Heat Deflection Temperature 0 45 Mpa 95 °C
    Vicat Softening Temperature 10 N 155 °C
    Melting Temperature 165 °C

    As an accredited SABIC PP Homopolymer 578P factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing SABIC PP Homopolymer 578P is supplied as free-flowing pellets in sealed 25 kg bags, palletized and shrink-wrapped for safe transport.
    Container Loading (20′ FCL) 20′ FCL container loaded with SABIC PP Homopolymer 578P, packed in 25kg bags on shrink-wrapped pallets, approximately 20 metric tons per shipment.
    Shipping SABIC PP Homopolymer 578P is shipped as free-flowing pellets in 25 kg bags, bulk bags, or silo trucks. It is non-hazardous under transport regulations but should be kept dry, protected from moisture, heat, and direct sunlight, and handled to prevent dust accumulation and contamination.
    Storage Store in a dry, clean, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers sealed to prevent moisture contamination and dust accumulation. Avoid contact with strong oxidizing agents. Maintain ambient temperatures and protect packaging from physical damage. No special storage hazards exist under normal conditions.
    Shelf Life Shelf life is indefinite when stored in original packaging, in a cool, dry, well-ventilated area away from UV light.
    Application of SABIC PP Homopolymer 578P

    Thin-wall dairy cups and margarine tubs are injection moulded from SABIC PP 578P at melt temperatures from 220 °C to 250 °C, with the hot runner manifold held at 230 °C to 245 °C. The grade’s nominal melt flow rate of 25 g/10 min (ASTM D1238, 230 °C, 2.16 kg) and density of 0.905 g/cm³ (ISO 1183-1) enable flow-length-to-wall-thickness ratios up to 200:1 in valve-gated multicavity tools when injection velocity is maintained above 150 mm/s and melt cushion is held at 3.0 mm to 5.0 mm. The core-to-wall thickness ratio in stacking moulds rarely exceeds 0.6 because the homopolymer solidifies rapidly at the cooled tool surface, producing a skin layer 0.08 mm to 0.12 mm thick that restricts pressure transmission to the core. On production-scale single-stage reciprocating screw machines with screw diameters from 32 mm to 50 mm and L/D ratios of 20:1 to 25:1, repeatable filling of 0.35 mm side walls has been documented only when the mould is vented along the full perimeter at intervals no greater than 40 mm and vacuum-assisted venting is applied. Shrinkage in thin-wall polypropylene homopolymer parts is anisotropic; side-wall shrinkage along flow is typically 1.0% to 1.4% and perpendicular shrinkage is 1.2% to 1.6% per ASTM D955, while the base rim may develop sink marks if pack pressure falls below 60% of peak injection pressure. Cooling water temperature is maintained at 10 °C to 30 °C, with turbulent flow characterized by Reynolds numbers greater than 10,000, to control post-mould crystallinity and dimensional stability during warehouse storage at up to 40 °C. Food-contact compliance for dairy applications is governed by FDA 21 CFR 177.1520 and EU 10/2011; overall migration under OM2 conditions (2 h at 70 °C, 3% acetic acid) must remain below 10 mg/dm². The grade is not intended for repeated impact at freezer temperatures below -10 °C; chilled distribution at 4 °C is acceptable only if the container side wall remains above 0.35 mm and the closure thread is not notched.

    Regulation / StandardApplicabilityConditional LimitTest Reference
    FDA 21 CFR 177.1520Olefin polymers in direct food contactPP homopolymer; extractable fraction per table21 CFR §177.1520(c)
    EU 10/2011Plastic materials in food contactOverall migration < 10 mg/dm² or 60 mg/kgEN 1186-1
    REACH (EC) No 1907/2006SVHC content in articlesNo SVHC above 0.1% w/wCandidate List
    RoHS 2011/65/EUElectrical/electronic equipmentPb, Hg, Cd, CrVI, PBB, PBDE limitsIEC 62321

    What Limits Torque Retention in Tamper-Evident Polypropylene Closures?

    Tamper-evident closures for carbonated soft drinks, bottled water and aseptic tea beverages are moulded from SABIC PP 578P on high-cavitation closure tools with conical gate inserts and continuous hot-runner systems. The grade’s tensile yield stress of approximately 35 MPa (ISO 527-2) and flexural modulus of approximately 1550 MPa (ISO 178) provide the structural stiffness necessary to maintain removal torque after application. Torque retention is limited by stress relaxation in the bridge elements that connect the shell to the tamper-evident band. At 23 °C and 50% relative humidity, injection-moulded bridges with cross-sectional dimensions of 0.5 mm by 0.6 mm exhibit a removal torque decay of up to 20% over 7 days when the closure is applied at 1.8 N·m to a PCO 1881 neck finish. This decay is governed by crystalline morphology: rapid cooling at mould temperatures from 10 °C to 25 °C generates a fine spherulitic skin but leaves a less ordered core, and post-mould secondary crystallisation at ambient temperature raises shrinkage and microstress at the bridge roots. Processing conditions for stable torque retention require a melt temperature of 230 °C to 250 °C, a hold pressure of 40 MPa to 60 MPa, and a hold time at least 1.5 times the gate freeze time to eliminate sink marks that reduce bridge section integrity. Mould release selection is critical; low-volatility food-grade releases are used because silicone-based external release agents can migrate to the closure sealing surface and reduce the coefficient of friction needed for unscrewing torque. Environmental stress cracking in acidified sugar solutions is not the primary limiting factor, but published data for this specific closure configuration is limited. Field failures have been observed not in the shell but in the tamper-evident band when the band is scored too deeply during slitting. Slitting depths above 0.45 mm on a 0.9 mm band reduce the band elongation at break below 8% (ASTM D638) and cause premature rupture during high-speed application. The application boundary is cold chain: PP homopolymer closures lose impact toughness at temperatures below 0 °C, and closures that must withstand -20 °C drop tests or carbonated beverage pressure at refrigeration temperatures below 2 °C require notched impact validation and may require blending with an impact copolymer.

    Diagnostic Pipette Tips Require Uniform Mould Fill at High Cavitation

    In laboratory consumables, SABIC PP 578P is used for non-optical pipette tips, microcentrifuge tubes and PCR tube strips where dimensional consistency across 48- to 96-cavity moulds is the overriding process requirement. The melt flow rate of 25 g/10 min permits filling of tip nozzle diameters as small as 0.4 mm at injection speeds up to 180 mm/s; however, because the nozzle region is a blind flow path, air entrapment and diesel burns occur if the mould is not evacuated to below 50 mbar absolute in the nozzle insert. On production lines, cavity-to-cavity fill imbalance is held below 2% by balancing the hot runner according to natural flow length, not by adjusting individual valve gate timing. Dimensional quality of pipette tips is evaluated by gravimetric mass distribution: for a 200 µL tip, a shot-to-shot mass variation of less than 0.8% and a cavity-to-cavity mass standard deviation of less than 0.15% are required to maintain suction volume accuracy within ±2%. PP homopolymer has a hydrophobic surface with water contact angle typically between 95° and 105° (sessile drop, ISO 19403-2), which reduces aqueous sample retention, but this also limits wetting of ink and is a constraint when longitudinal labeling is required. The material is not recommended for gamma sterilisation at doses above 25 kGy; polypropylene undergoes oxidative chain scission under ionising radiation, leading to measurable loss in tensile elongation at break and yellowing that can exceed 10 yellowness index units after 40 kGy. Ethylene oxide sterilisation is compatible, provided residual ethylene oxide after aeration meets ISO 10993-7 limits. Autoclaving at 121 °C for 30 min is possible only for articles with supported geometry; because heat deflection temperature under 0.45 MPa load (ISO 75-2/B) is approximately 95 °C, unsupported pipette tip racks may distort beyond the flatness tolerance of 0.2 mm during steam sterilisation.

    When Hot-Fill Temperatures Approach 90 °C for Barrier-Lined PP Homopolymer Trays

    Hot-fill trays and microwaveable containers with polypropylene homopolymer structural layers and EVOH barrier inserts are processed with a temperature boundary defined by heat deflection temperature and creep behaviour of the PP homopolymer. The 0.45 MPa HDT of SABIC PP 578P is approximately 95 °C (ISO 75-2/B); therefore hot-fill at 85 °C to 90 °C is tolerated for hold times below 10 min only if the sidewall geometry includes vertical ribs and the filling line does not apply top load exceeding 1.5 kg per tray during sealing. Above 90 °C, flexural modulus declines below 600 MPa, and creep modulus under a 2 MPa sustained load after 30 min at 95 °C can fall below 400 MPa, resulting in wall deflection greater than 1.0 mm and seal distortion. The processing conflict in barrier-lined trays is the adhesion temperature window of the tie resin: coextruded or thermoformed structures use maleic anhydride-grafted polypropylene tie layers that require PP surface temperatures above 160 °C during lamination, but prolonged exposure above 250 °C in the extruder degrades the homopolymer’s molecular weight and shifts melt flow rate upward by more than 15%. Therefore the extruder profile for the PP skin layer is set with zone temperatures from 200 °C to 230 °C, and the melt is kept below 245 °C at the die. SABIC PP 578P serves the structural function in these trays, not the oxygen barrier function; the oxygen transmission rate of PP homopolymer alone is approximately 1500 cm³/m²·day·atm at 23 °C, 0% RH, reduced to below 1 cm³/m²·day·atm only by the EVOH layer. Retort applications above 100 °C are outside the grade’s operating window; published data for this specific configuration is limited, but steam retort at 121 °C for 20 min is not recommended because the PP homopolymer enters the rubbery plateau and the EVOH barrier loses oxygen barrier after moisture uptake.

    Rigid housewares and storage containers manufactured from SABIC PP 578P encompass stackable crates, utility boxes, drawer dividers and closures for household chemical bottles. These parts are typically injection moulded with wall sections from 1.5 mm to 3.0 mm, which is thicker than thin-wall packaging and introduces sink-mark control as the dominant quality constraint. Pack pressure is maintained at 50% to 70% of peak cavity pressure until the gate freezes; for a 2.5 mm wall section, gate freeze time can be 8 s to 12 s, and total cycle time is governed by the part’s thickest rib. The homopolymer’s tensile yield stress of approximately 35 MPa (ISO 527-2) and flexural modulus of approximately 1550 MPa (ISO 178) give stackable crates sufficient top-load resistance at 23 °C; however, the grade is not intended for heavy-duty industrial crates that require falling dart impact at temperatures below 0 °C. Chemical resistance in household applications is narrow but well characterised: immersion in 5% sodium hydroxide at 60 °C for 1000 h typically produces less than 5% loss in tensile stress at yield, but strong oxidising acids and halogenated solvents are incompatible and cause surface cracking or swelling. For toys and childcare articles, compliance requires EN 71-3 migration limits for specific elements and REACH Annex XVII restrictions; the grade is used only in applications without small detachable parts that could present a choking hazard. Living hinges are not a recommended design feature for this high-flow homopolymer because the low molecular weight orientation in the hinge region leads to fatigue failure below 10,000 flex cycles, whereas a lower-MFR polypropylene homopolymer would be required for durable living hinges.

    Chemical Resistance in White Goods and Pump Components

    In washing machine detergent dispensers, pump housings and dishwasher spray arms, SABIC PP 578P is exposed to alkaline detergents, bleach, rinse aids and water at elevated temperature. The polypropylene homopolymer offers resistance to hydrolysis and to aqueous sodium hydroxide at concentrations up to 5% at 60 °C; however, the limiting factor is bleach-induced oxidative degradation. Sodium hypochlorite at 2% available chlorine, 40 °C, 500 h, reduces elongation at break from approximately 8% to below 3% (ASTM D638) when the part is under continuous flexural stress above 10 MPa. Therefore detergent dispenser mounts with snap-fits must be designed so outer fibre strain does not exceed 0.8% after assembly. Processing for these thicker components uses melt temperatures from 220 °C to 240 °C and mould temperatures from 20 °C to 45 °C; higher mould temperatures above 40 °C reduce internal stress and improve environmental stress crack resistance but lengthen cooling time and may increase cycle time by 10% to 15%. When moulding pump components with screw threads and O-ring grooves, the grade’s shrinkage of 1.2% to 1.8% (ASTM D955) must be compensated by tooling adjustment; weld lines at the pump inlet can reduce tensile strength by 25% to 35% if the knit line is formed by two fronts at low melt temperature. The grade is not recommended for continuous exposure to water above 80 °C under pressure because creep and oxidation shorten the functional lifetime below the typical 5000 h appliance reliability target. For electrical enclosure parts in white goods, the material is rated UL 94 HB unless flame retardant additives are used; the base homopolymer is not V-2 or 5VA rated and must not be substituted for flame-retardant PP grades in uninterruptible power supply or power tool housings.

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    Certification & Compliance
    More Introduction

    SABIC PP Homopolymer 578P is a controlled-rheology polypropylene homopolymer supplied as cylindrical pellets for sheet extrusion, thermoforming, and profile converting operations. The numeric suffix 578P identifies a medium-viscosity product within the SABIC PP homopolymer portfolio. When measured at 230°C under a 2.16 kg piston load in accordance with ISO 1133-1:2022, the nominal melt flow rate is 2.0 g/10 min. Density at 23°C is 0.905 g/cm³ when determined by ISO 1183-1:2019. The base stabilization package is formulated for repeated extrusion heat histories, but the standard grade does not incorporate an intentional slip or antiblock additive. Modification of surface friction by dry blending slip masterbatch at the hopper is not recommended for this grade because gravimetric feeder let-down variation shifts the coefficient of friction and alters thermoforming release. The material is unpigmented and is not UV-stabilized for long-term outdoor exposure; converters targeting outdoor service must compound an appropriate hindered amine light stabilizer package or carbon black at a loading sufficient to achieve the required accelerated weathering classification.

    Which Normative Property Set Defines the 578P Grade?

    The typical mechanical and thermal property envelope is summarized below. Values are extracted from standard specimen testing and do not constitute lot-release specifications. Lot acceptance is governed by melt flow rate, ash content, and contamination limits agreed between the supplier and converter.

    PropertyTest MethodTypical Value
    Melt flow rate (230°C/2.16 kg)ISO 1133-1:20222.0 g/10 min
    Density (23°C)ISO 1183-1:20190.905 g/cm³
    Tensile stress at yieldISO 527-2:201235 MPa
    Tensile elongation at yieldISO 527-2:201210%
    Flexural modulusISO 178:20191500 MPa
    Notched Izod impact strength (23°C)ISO 180/A:20193.5 kJ/m²
    Vicat softening temperature (A50)ISO 306:2022155°C
    Heat deflection temperature (0.45 MPa)ISO 75-2:201395°C

    Processing converters running sheet lines should select a single-screw extruder with a barrier screw and L/D between 24:1 and 30:1. A compression ratio of 3:1 is a typical starting point for medium-MFR polypropylene. Feed-throat temperature should be controlled below 60°C; higher feed-throat temperatures soften pellet surfaces and increase the risk of bridging. Barrel zones from feed to metering are commonly set at 200°C, 220°C, and 230°C, with adapter and flat-die zones at 230°C and 235°C. The melt temperature measured with an immersion probe should remain within 225–245°C. Above 250°C oxidative chain scission reduces melt viscosity, shifts the MFR upward, and produces yellowing in unpigmented sheet. Die-lip deposit formation on polished chrome-plated die lips accelerates with extended runs above this threshold; published data for 578P-specific campaigns is limited, but the degradation threshold is consistent with the onset of polypropylene thermo-oxidative degradation. Residence time at melt temperatures above 230°C should be limited to 15 min to control melt flow drift. Frequent purging with a medium-MFR high-density polyethylene or a commercial purging compound at shutdown reduces carbonized deposit accumulation.

    Pre-drying is not required for hydrolysis prevention because polypropylene is nonhygroscopic. Surface condensation from pallets stored at relative humidity above 60% can generate splay or surface pitting in extruded sheet. In those conditions, pellets should be dried at 80°C for 2 h in a desiccant dryer with a dew point no higher than -30°C.

    Rheologically, the zero-shear viscosity of a 2.0 g/10 min homopolymer at 230°C is generally higher than that of grades with MFR above 8 g/10 min. Extruder drive sizing for 578P sheet lines should allow for specific energy input of 0.25–0.35 kW/(kg/h); undersized motors limit screw speed and increase melt residence time. The higher melt strength reduces sag in vertical sheet take-off, but die pressure at a given throughput will be greater than for high-flow grades. Shear heating must be controlled through screw speed and screen-pack selection; a 60/120/60 mesh breaker-plate pack is adequate for sheet thicknesses down to 0.5 mm. At shear rates above 1000 s-1, sharkskin melt fracture may appear in thin-gauge sheet, depending on die land length and melt temperature. Raising melt temperature above 250°C to eliminate melt fracture conflicts with degradation stability; instead, die land length or draw-down ratio should be adjusted.

    In sheet extrusion, gauge bands along the machine direction often arise from die bolt misalignment, roll deflection, or nonuniform melt temperature across the die width. A thermocouple grid across the die exit can identify temperature differences greater than 5°C, which may require die-zone trim adjustment. Roll deflection in a three-roll stack should be corrected by roll crown or cross-axis adjustment before altering the die gap. Optical defects such as sharkskin are usually melt fracture or melt temperature-related, while splay or surface pitting is linked to surface moisture or contamination. Because 578P is translucent in natural form, haze measurement per ASTM D1003 on 1 mm sheet can be used to track contamination; increases above the baseline value indicate degraded material, regrind contamination, or excessive melt temperature.

    Incoming resin QC should include melt flow rate per ISO 1133-1:2022 and density per ISO 1183-1:2019. Lot-to-lot MFR variation is typically controlled to ±0.3 g/10 min around the nominal 2.0 g/10 min. If MFR exceeds 2.5 g/10 min, melt strength decreases and thermoforming sag may become unacceptable; if MFR falls below 1.5 g/10 min, extruder amperage and die pressure increase, and throughput may be limited by motor load. Published lot-specific historical data for 578P is limited; converters should establish internal control limits from incoming shipments.

    The processing window is constrained by two opposing boundaries: the lower melt temperature limit for surface gloss and the upper limit for thermal degradation. At melt temperatures below 220°C, the sheet may show high orientation and thickness variation due to insufficient relaxation; at melt temperatures above 250°C, degradation shifts MFR and increases die-lip deposit. Operators should use a melt-temperature immersion probe rather than relying on barrel set points, because shear heating can create differences of 10–15°C between set point and actual melt temperature at high screw speeds.

    When Low Melt Flow Rate Stabilizes Sheet Gauge Control

    Flat-die extrusion of 578P for deep-draw thermoforming uses the low MFR to maintain sheet gauge uniformity across the die width. A coat-hanger die with adjustable restrictor bars and a polished three-roll stack is the standard downstream configuration. Roll temperatures of 20°C, 30°C, and 40°C from first to third roll are common for homopolymer sheet in the 0.8–1.5 mm thickness range. The sheet surface temperature at the forming station should be maintained at 160–165°C for male-tool forming. Below 155°C, forming force increases and springback becomes measurable; above 168°C, gloss reduction and wall-thickness nonuniformity occur. As a homopolymer, 578P has a narrower thermoforming window than random copolymers, and deep-draw ratios above 2.5:1 generally require plug assist with heated syntactic foam or thermoset plugs. Plug temperature control is critical; plug temperatures below 90°C can produce chill marks, while plug temperatures above 120°C can cause local thinning. The absence of ethylene comonomer also reduces low-temperature impact performance of formed articles; applications requiring ductile behavior below 0°C should be re-evaluated with a heterophasic copolymer grade.

    Comparative property data from capillary rheometry and standard specimen testing illustrate the positioning of 578P among polypropylene products. High-flow injection molding homopolymers with MFR above 12 g/10 min produce shorter fill times and lower cavity pressures in thin-wall injection molding, but their lower melt strength makes them unsuitable for unsupported sheet take-off. Controlled-rheology grades such as 578P exhibit a narrower molecular weight distribution than conventional reactor grades of similar MFR, leading to reduced die swell and more predictable die-lip opening compensation. Compared with random copolymers, 578P offers a higher Vicat softening temperature of 155°C according to ISO 306:2022, whereas typical random copolymer grades fall between 125°C and 135°C. The trade-off is lower notched Izod impact strength; a value of 3.5 kJ/m² at 23°C per ISO 180/A:2019 is below the ≥8 kJ/m² commonly reported for heterophasic impact copolymers at the same temperature. Unfilled homopolymer should not be specified for continuous load-bearing service at temperatures above 80°C without creep rupture evaluation. For chemical contact, polypropylene homopolymer resists many dilute acids and bases, but strong oxidizing acids, chlorinated solvents above 60°C, and aromatic hydrocarbons can swell or degrade the surface; specific chemical compatibility should be tested under service conditions.

    Recovery of edge trim and thermoformed skeletons is common in sheet operations. Clean regrind of 578P can be incorporated at levels up to 30% without significant loss of properties if the regrind is free of paper labels, adhesive residues, and moisture. Higher regrind levels reduce melt strength and shift the effective MFR upward because of repeated heat history; converter trials should determine the maximum acceptable level for a specific draw ratio. Contact with copper or copper alloys at melt temperatures above 250°C should be avoided because copper ions catalyze thermo-oxidative degradation of polypropylene.

    Injection molding of 578P is technically possible for thick-wall parts but is not the primary intended converting route. Melt temperature should be set at 230–250°C; mold surface temperature between 20°C and 50°C controls crystallinity and shrinkage. Injection pressure and holding pressure should be determined by mold-flow simulation; starting values of 80–120 MPa hydraulic pressure are typical for medium-MFR homopolymers but must be reduced for hot-runner systems to prevent drool. Because of the low MFR, thin-wall sections below 1.0 mm may show incomplete filling unless high-speed injection is available. The material is not recommended for applications requiring repeated flexural endurance without specific long-term flexural fatigue evaluation.

    Regulatory Compliance Matrix for Food-Contact and Industrial Conversion

    Compliance is assessed against the regulatory frameworks relevant to sheet and thermoformed food packaging. The base resin complies with the compositional requirements of FDA 21 CFR 177.1520 for polypropylene articles intended for food contact, subject to end-use conditions and migration testing performed by the converter. Under EU Regulation (EU) No 10/2011, overall migration from the final article must not exceed 10 mg/dm² of food-contact surface area. REACH compliance is documented under Regulation (EC) No 1907/2006; substances of very high concern are not intentionally added above the 0.1% w/w communication threshold. RoHS Directive 2011/65/EU limits lead, mercury, hexavalent chromium, PBB, and PBDE to 0.1% w/w and cadmium to 0.01% w/w in homogeneous materials.

    FrameworkRelevant DesignationLimit/Condition
    EU food contactEU Regulation (EU) No 10/2011Overall migration 10 mg/dm²
    U.S. food contactFDA 21 CFR 177.1520Conditions of use A–H; converter verification required
    REACHRegulation (EC) No 1907/2006SVHC not added above 0.1% w/w
    RoHSDirective 2011/65/EUPb, Hg, Cr(VI), PBB, PBDE 0.1% w/w; Cd 0.01% w/w

    The converter is responsible for validating final-article migration under the intended food-contact conditions.

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