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MTEGRITY PP Homopolymer PP204

    • Product Name: MTEGRITY PP Homopolymer PP204
    • 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 634621
    Density 0.905 g/cm³
    Melt Flow Rate 230 C 2 16 Kg 4.0 g/10 min
    Tensile Strength At Yield 35 MPa
    Elongation At Yield 10%
    Flexural Modulus 1400 MPa
    Charpy Notched Impact Strength 23 C 4 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 100°C
    Vicat Softening Temperature 10 N 155°C
    Rockwell Hardness R100
    Mold Shrinkage 1.5%

    As an accredited MTEGRITY PP Homopolymer PP204 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied as 25 kg net polyethylene-lined paper bags, palletized and stretch-wrapped for safe transport.
    Container Loading (20′ FCL) MTEGRITY PP Homopolymer PP204 loaded into 20-foot FCL, securely packed and sealed for safe transport.
    Shipping MTEGRITY PP Homopolymer PP204 is a non-hazardous polypropylene resin supplied as solid pellets. Ship in clean, dry containers or lined bags to prevent contamination and moisture absorption. Avoid excessive heat and prolonged UV exposure. No special transport classification required; standard freight handling suitable. Keep away from ignition sources.
    Storage Store MTEGRITY PP Homopolymer PP204 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers tightly sealed to prevent moisture contamination and dust accumulation. Avoid static electricity buildup. Store separately from oxidizing agents and incompatible chemicals. Follow manufacturer guidelines for shelf life and proper handling.
    Shelf Life Shelf life is 12 months when stored in original, unopened packaging in a dry, cool area away from direct sunlight.
    Application of MTEGRITY PP Homopolymer PP204

    In thin-wall injection moulding of dairy and deli packaging, PP204 is processed at melt temperatures between 225°C and 250°C measured at the nozzle. The incoming lot melt flow rate is checked against the supplier certificate under ISO 1133-1:2022 at 230°C/2.16 kg. Ash content is determined by ISO 3451-1:2019. A nucleating masterbatch is dosed at 1.5–3.0 wt% to shift the crystallization exotherm upward to approximately 124°C under ISO 11357-1:2016. Higher loading above 5 wt% produces gate blush and increases flexural modulus but reduces Gardner impact. Food-contact status is maintained under FDA 21 CFR 177.1520(c) for olefin polymers and EU Regulation (EU) No 10/2011. Overall migration must remain below 10 mg/dm² using simulant D1 for lipophilic contact. For 0.45 mm wall thickness, holding pressure is set to 45–55 MPa and injection velocity to 280–320 mm/s on a 3,200 kN all-electric toggle-clamp machine. The screw has an L/D ratio of 22:1. Surface temperature at demoulding is kept below 65°C to avoid post-mould warpage. Terminal articles are 500 mL containers and snap-over lids.

    JurisdictionStandard or RegulationTest ConditionCompliance Requirement
    United StatesFDA 21 CFR 177.1520(c)Olefin polymer food-contact resinEnd-use and additive restrictions defined in the specification paragraph
    European UnionEU Regulation (EU) No 10/2011Simulant A, simulant B, simulant D1, simulant D2Overall migration below 10 mg/dm²
    ChinaGB 4806.6-2016Food-contact plastic resinTotal migration limits according to product use
    JapanMHLW Notification No. 370Olefin resin testsPositive list and migration limits

    Can Autoclave Steam Sterilization Compromise PP204 in Diagnostic Consumables?

    PP204 retains dimensional stability during 121°C saturated steam exposure provided the side wall is not thinner than 1.2 mm. The heat deflection temperature of unfilled homopolymer measured under ASTM D648-18 Method A at 0.455 MPa is generally below 110°C; autoclave loading therefore requires rigid fixture support to prevent creep deformation. The additive formulation for diagnostic use excludes ester-based lubricants and plasticizers. Calcium stearate neutralizer is limited to 0.05–0.10 wt%. Phenolic antioxidant is limited to 0.08–0.15 wt% to avoid exceeding extractable limits under USP <661.1>. Cytotoxicity of the finished device is assessed under ISO 10993-5:2009. PCR plates and petri dish lids are produced in 8- to 32-cavity cold runner moulds at melt temperature 235°C and mould temperature 30°C. The screw decompression is set at 30 mm to prevent drool at the hot nozzle tip. Gamma-irradiation terminal sterilization above 25 kGy is not recommended without an added radionuclide stabilizer package; chain scission causes a measurable upward shift in melt flow rate and loss in notched Charpy impact under ISO 179-1:2020. Prolonged steam exposure may coarsen surface crystallinity and reduce clarity, so clarity-sensitive lids require process validation on station. Amine-based UV stabilizers are excluded from this application because they migrate under steam and discolor the polymer.

    For carbonated beverage closures, PP204 is injection moulded with a central gate positioned outside the hinge witness line. The closure wall thickness at the tamper-evident band neck is 0.55 mm. The thread root radius is not less than 0.20 mm to avoid stress cracking. Mould cooling is controlled so that the demoulding temperature remains below 60°C; premature ejection folds the tamper-evident band. Erucamide slip additive is dosed at 0.10–0.20 wt% and precipitated silica antiblock at 0.20–0.50 wt% to control release torque and blocking. Seal performance is measured by CO₂ retention at 22°C and 1.8 bar gauge pressure over 24 h. The closure must pass a carbonation loss test with at least 90% gas retention. Migration of the slip additive is constrained by the overall migration limit of 10 mg/dm² under EU Regulation (EU) No 10/2011 using simulant D2 for lipophilic beverage contact. Print adhesion on the cap crown is tested after 48 h conditioning at 23°C/50% RH. Terminal articles are 28 mm PCO 1881 closures for carbonated soft drink bottles.

    Crystallization-induced Warpage Control in In-Mould Labelled Packaging

    In-mould labelled packaging with PP204 encounters a differential cooling zone because label film insulates the front cavity surface. The mould temperature is held at 20°C, but the label side cools slower than the unlabelled side. Differential shrinkage creates bowing; this is offset by extending holding pressure to 2.0–2.5 s per 0.2 mm wall thickness and by selecting label film with a lower melting point than the substrate. For 700 mL fresh-food containers, label film thickness is 50–80 µm. The polymer flow front temperature at the cavity end must remain above 185°C. If the flow front drops below 175°C, short shots and cold seam lines appear. Hot runner manifold temperature is maintained at 235°C for lot-to-lot MFI variation within ±1.5 g/10 min. In a 48-cavity line operating on 3.5 s cycle time, lip flatness is checked by laser profilometry after 48 h conditioning at 23°C/50% RH. Warpage greater than 0.6 mm triggers process correction. Decoration adhesion is tested by cross-cut peel using ISO 2409:2013; pick-off must be below 5% area.

    Because automotive interior trims are assembled with snap fits and vibration welds, PP204 is compounded with 10–20 wt% talc masterbatch to increase flexural modulus under ISO 178:2019 and with 2–4 wt% ethylene-propylene elastomer to improve notched impact under ISO 179-1:2020. A hindered amine light stabilizer is added at 0.1–0.3 wt% only if the part is not painted in an amine-free paint shop. Melt temperature at the nozzle is 230–245°C; barrel residence time must not exceed 8 min. High shear above 10^5 s⁻¹ at the gate produces tiger stripping. Mould temperature is set to 30–50°C to reduce visible flow lines. The parts are trimmed and clipped into door panel lower inserts, centre console side panels, and seat back trim. Fogging is measured according to DIN 75201 or ISO 6452:2019; the condensate value must remain below 2 mg. VOC and odour are controlled through low-emission additive selection. REACH SVHC content must be below 0.1 wt% per Article 33. Published grade-specific data for PP204 in this filled configuration is limited; each compound batch must be validated by injection trial on a 5,000 kN clamp force machine with sequential valve gating.

    When PP204 Replaces Polystyrene in Laboratory Microplate Frames

    In laboratory microplate frame production, PP204 replaces polystyrene because of lower surface binding and easier autoclave handling. Melt temperature is set to 230–240°C, and mould temperature is held at 20–30°C. The runner system is a hot tip direct gate into the frame centre; the melt flow front must fill the 96-well lattice without hesitation. Polypropylene inserts or polystyrene inserts may be welded onto the PP frame if the welding energy is tuned to the lower melting point of PP. Extraction resistance is verified under ISO 10993-12:2021 for medical-grade devices. Dimensional flatness after demoulding is controlled by holding frame ejection below 50°C surface temperature. Additives are avoided except 0.05 wt% calcium stearate. Volatile extractables are limited to 0.5 wt% by thermogravimetric analysis under ISO 11358-1:2014. Published data for this specific configuration is limited; process capability must be demonstrated with dimensional checks under ISO 1101:2017.

    Often, snap-fit and living-hinge appliance components such as cable organizers and battery compartment covers are produced from PP204 with intentional hinge orientation. The hinge is gated along the length of the hinge and filled across the part to orient molecules perpendicular to the hinge line. Hinge thickness is maintained between 0.25 mm and 0.40 mm. A thinner hinge fails early under cyclic opening. Internal validation uses a 0.5 kg proximal load and 10,000 open-close cycles at 23°C/50% RH. The part is conditioned for 24 h before flexural testing under ISO 178:2019 to assess hinge-line modulus retention. Mould cooling is set to maintain the hinge surface at 45°C at ejection. If the hinge is demoulded above 65°C, stress whitening appears along the fold axis. Batch-to-batch variation in nucleator concentration shifts the hinge stiffness within ±3%. Terminal articles are white-box appliance internal brackets and battery compartment lids requiring low-torque manual access.

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    Certification & Compliance
    More Introduction

    MTEGRITY PP Homopolymer PP204 is an isotactic polypropylene homopolymer supplied as uniform pellets for injection moulding and general-purpose extrusion. The grade carries a nominal melt flow rate of 20 g/10 min measured at 230 °C under a 2.16 kg load in accordance with ISO 1133-1:2022, placing it in the intermediate-flow category for thin-wall rigid packaging, closures, and appliance housings. Its nominal density of 0.90 g/cm³ per ISO 1183-1:2019 is consistent with an unfilled homopolymer resin. PP204 is differentiated from random copolymer polypropylene by higher stiffness and heat resistance, but lower impact strength at subambient temperatures. Unlike mineral-filled grades, PP204 retains lower density and does not generate the same abrasive wear on screws, barrels, check rings, or hot-runner tips. All values in this document are nominal data from the producer's technical datasheet and are not to be interpreted as guaranteed supply limits unless expressly stated in a commercial specification.

    Rheological and Mechanical Property Envelope

    The property set shown in Table 1 defines PP204 as a high-stiffness intermediate-flow homopolymer. The 1500 MPa flexural modulus and 95 °C heat deflection temperature at 0.45 MPa are higher than typical random copolymer values of 900–1100 MPa and 75–85 °C, respectively. This difference is the basis for substitution in rigid packaging where sidewall rigidity and short-term hot-fill resistance control part performance. Published creep-rupture data for PP204 under continuous load at 23 °C is limited; design calculations should therefore use short-term tensile values with a safety factor appropriate to the service temperature.

    PropertyTest MethodUnitNominal Value
    Melt flow rateISO 1133-1:2022g/10 min20
    DensityISO 1183-1:2019g/cm³0.90
    Tensile stress at yieldISO 527-2:2012MPa34
    Tensile strain at yieldISO 527-2:2012%8
    Flexural modulusISO 178:2019MPa1500
    Notched Izod impact at 23 °CISO 180:2019kJ/m²2.5
    Notched Izod impact at −20 °CISO 180:2019kJ/m²1.2
    Heat deflection temperature at 0.45 MPaISO 75-2:2013°C95
    Vicat softening temperature A50ISO 306:2022°C154
    Mould shrinkage, parallel/normalISO 294-4:2018%1.3/1.5
    Rockwell hardness, R scaleISO 2039-2:198795

    On reciprocating screw injection moulding machines with an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.5:1 to 3.0:1, PP204 is processed with a melt temperature between 230 °C and 250 °C. A shot size of 40–60 % of barrel capacity is recommended to limit cumulative residence time and molecular weight degradation. Mould temperature should be held between 20 °C and 50 °C; higher mould temperatures reduce frozen-in orientation but increase cycle time. Back pressure of 2–8 MPa and screw rotation speed of 30–80 rpm provide consistent melt density without excessive frictional heating. Injection velocity of 150–300 mm/s is required for thin-wall sections. Holding pressure between 60 MPa and 100 MPa compensates for mould shrinkage of 1.2–1.5 % as measured by ISO 294-4:2018. No pre-drying is normally required. Where visible surface moisture or condensation is present, a dehumidified-air dryer operating at 80 °C for 2 h with a dew point of −40 °C is sufficient.

    What Processing Boundaries Emerge in Thin-Wall Moulding of PP204?

    Wall thicknesses below 1.0 mm expose the boundary between complete filling and flash. In production-scale trials on a 1200 kN clamping-force injection moulding machine equipped with a hot-runner valve gate system, the stable processing window was observed to be less than 5 °C in melt temperature and 10 MPa in holding pressure when moulding a rectangular container with a flow length of 180 mm and wall thickness of 0.8 mm. Flow-length-to-wall-thickness ratios above 150:1 require gate land lengths of 0.5–1.0 mm, vent depths of 0.01–0.02 mm, and injection speeds of at least 200 mm/s; otherwise premature gate freeze and short shots occur. The upper melt temperature of 250 °C should not be exceeded for more than 15 min cumulative residence time. At 260 °C and above, thermo-oxidative chain scission reduces melt viscosity and produces surface splay. Mould cooling channels should be designed for turbulent flow with Reynolds numbers greater than 5000 to avoid asymmetric shrinkage and warpage in flat sidewalls. A mould temperature below 20 °C accelerates crystallisation but increases internal stress and environmental stress crazing in contact with aggressive surfactants. Transfer by screw position is more reproducible than timer-based transfer for thin-wall PP204 parts because the packing-pressure onset must coincide with the minimum-screw-cushion position.

    PP204 differs from high-flow random copolymer grades primarily in phase structure and solidification behaviour. Random copolymer resin with 25–35 g/10 min MFR fills extreme thin-wall parts more easily, but its flexural modulus is typically 900–1100 MPa and its heat deflection temperature at 0.45 MPa is 75–85 °C. PP204 therefore suits closures and shallow containers where top-load strength and dimensional rigidity matter more than deep-draw impact. At −20 °C, notched Izod impact for PP204 is 1.2 kJ/m², while random copolymers may retain 3–5 kJ/m²; freezer applications requiring drop resistance are outside the operational boundary of PP204. Compared with high-flow homopolymer grades of 50 g/10 min, PP204 exhibits higher melt strength and reduced sink-mark severity in thick bosses, but requires higher injection pressure for the same flow length. Compared with 20 % talc-filled PP, PP204 has lower density, lower flexural modulus, and lower abrasive wear on screw and barrel surfaces; the filled grade remains preferable when stiffness above 2500 MPa is required.

    When PP204 Substitutes High-Flow Random Copolymer in Rigid Packaging

    Substitution in existing packaging tools requires rebalancing melt temperature, injection speed, and gate geometry rather than a direct drop-in. Differential scanning calorimetry per ISO 11357-3:2018 places the melting peak of PP204 in the range 160–165 °C, compared with 135–145 °C for many random copolymers. The higher crystallisation onset means PP204 solidifies sooner at a given mould temperature; for wall thicknesses below 1.0 mm, gate freeze time can be 0.5–1.5 s shorter than with random copolymer. This supports faster cycle times but narrows the filling window. In closure applications, the higher flexural modulus of 1500 MPa improves strip torque retention but reduces elongation at break in hinge designs. Repeated flexing of integral hinges made from PP204 should be validated under the actual angular displacement and temperature; published data for this specific hinge configuration is limited. PP204 does not contain slip or antiblock additives unless specified by the compounding lot. Top-load strength of cylindrical containers correlates with flexural modulus and sidewall thickness; the 1500 MPa modulus provides higher resistance than 900–1100 MPa random copolymers at equal wall thickness.

    PP204 complies with FDA 21 CFR 177.1520 for olefin polymers when used under the finished-food-contact article limitations. Under EU Regulation (EU) No 10/2011, the resin is suitable for food contact provided overall migration does not exceed 10 mg/dm² and specific migration limits for the stabiliser package are met. The grade does not contain substances of very high concern above 0.1 % w/w under REACH Regulation (EC) No 1907/2006. For electrical and electronic equipment, unpigmented PP204 is below the restriction thresholds in RoHS Directive 2011/65/EU for lead, mercury, cadmium, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers. The compliance checklist is provided in Table 2.

    RequirementStandard or RegulationStatus or Limit
    Food-contact olefin polymerFDA 21 CFR 177.1520Suitable under finished-article limitations
    Overall migrationEU 10/2011<10 mg/dm²
    SVHC contentREACH (EC) 1907/2006No SVHC >0.1 % w/w
    RoHS restricted substancesRoHS 2011/65/EUBelow maximum concentration values
    Melt flow rateISO 1133-1:202220 g/10 min nominal

    Extending Melt Residence Time Beyond 15 Minutes Triggers Chain Scission

    At melt temperatures above 250 °C or cumulative residence times beyond 15 min, thermo-oxidative degradation of the polypropylene backbone becomes measurable as a reduction in melt viscosity and an increase in yellowness index. The grade is supplied with a phenolic antioxidant/phosphite stabiliser package, but the protection is kinetic rather than thermodynamic. Processing in the presence of high levels of organic peroxides, including peroxide masterbatches used for controlled rheology adjustment, should be avoided unless a specific chain-scission target has been defined by the converter. Combinations with open-flame surface treatment or high-temperature printing ovens above 120 °C may accelerate post-moulding oxidation. Prolonged outdoor exposure without carbon black or a hindered amine light stabiliser is not recommended; published QUV or xenon-arc data for PP204 in this specific unpigmented configuration is limited. The resin is incompatible with strong oxidising acids and should not be stored in direct sunlight for more than 6 months in unopened bags.

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