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Polypropylene Thin-wall Injection Grade PP M600X

    • Product Name: Polypropylene Thin-wall Injection Grade PP M600X
    • Factroy Site: Ningdong Energy and Chemical Industry Base, Yinchuan City, Ningxia
    • Price Inquiry: sales4@liwei-chem.com
    • Manufacturer: Ningxia Baofeng Energy Group Co., Ltd
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    Specifications
    HS Code 909486
    Density G Cm3 0.90
    Melt Flow Rate 230c 2 16kg G 10min 60
    Tensile Strength At Yield Mpa 35
    Tensile Elongation At Break Percent 10
    Flexural Modulus Mpa 1500
    Notched Izod Impact Strength 23c J M 25
    Heat Deflection Temperature 0 45mpa C 105
    Vicat Softening Temperature C 150
    Rockwell Hardness R Scale 95
    Mold Shrinkage Percent 1.2-1.8
    Melting Temperature C 165
    Water Absorption Percent <0.01

    As an accredited Polypropylene Thin-wall Injection Grade PP M600X factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Polypropylene Thin-wall Injection Grade PP M600X is supplied in 25 kg moisture-proof woven bags, 40 bags per pallet.
    Container Loading (20′ FCL) Loaded in 20-foot FCL: Polypropylene Thin-wall Injection Grade PP M600X in 25 kg bags, palletized and secured for export.
    Shipping Polypropylene Thin-wall Injection Grade PP M600X is supplied as odorless thermoplastic pellets in 25 kg moisture-proof bags, palletized and stretch-wrapped. Ship in clean, dry, ventilated containers at ambient temperature, avoiding direct sunlight, moisture, and ignition sources. Non-hazardous; no special dangerous-goods labeling required.
    Storage Store Polypropylene Thin-wall Injection Grade PP M600X in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and strong oxidizing agents. Keep material in original, closed packaging to prevent moisture and contamination. Avoid prolonged outdoor exposure and physical damage to bags. Maintain good housekeeping to control dust and static; use first-in, first-out stock rotation.
    Shelf Life Typical shelf life is 24 months when stored unopened in a cool, dry, well-ventilated area, protected from direct sunlight and moisture.
    Application of Polypropylene Thin-wall Injection Grade PP M600X

    Polypropylene M600X thin-wall injection grade enters chilled dairy and deli container programs as the base resin in high-cavitation stack molds producing tapered round and rectangular tubs. The applicable compliance structure includes EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² for food simulants, FDA 21 CFR 177.1520 for polyolefin materials, and China GB 4806.7-2023 for total migration and potassium permanganate consumption. The certificate of analysis for each lot should confirm melt flow rate under ISO 1133-1:2022; if the MFR falls below 50 g/10 min, thin-wall fill pressures rise and the packing window narrows. The formulation at the throat of the press is metered as 100 parts by weight of M600X with 1.5–3.0 phr white TiO₂ masterbatch and 0.05–0.2 phr nucleating masterbatch; slip/antiblock masterbatch is added at 0.5–2.0 phr when denesting force measured on a universal tensile tester at 50 mm/min must remain below 5 N per stack of 10 containers. On the production floor, high-speed injection molding machines with a 20:1–25:1 L/D general-purpose screw, compression ratio 2.0:1–2.5:1, and a shut-off nozzle are run at a melt temperature of 230–250°C, a chilled mold temperature of 15–40°C, an injection speed of 250–500 mm/s, and a packing pressure of 30–50 MPa. The processing conflict observed on high-cavitation tools is sink formation at stacking ledges and at the sidewall-base transition; below 0.40 mm wall thickness the packing channel freezes before compensation is complete, producing weight variation above ±2.0% across 96-cavity tools. Pre-drying is not normally required for natural resin stored under covered conditions, but surface moisture at relative humidity above 60% demands a desiccant dryer at 80–90°C for 2–4 h to avoid splay and flow marks. Terminal products include 150–500 mL dairy cups, 250–750 mL delicatessen containers, and recloseable takeout bases with snap-on lids produced at cycle times of 4–8 s.

    Food-contact compliance checklist for PP M600X thin-wall applications
    Standard / regulationJurisdiction / scopeRelevant clause or methodKey limit or condition
    EU Regulation (EU) No 10/2011Food contact plasticsAnnex I, Annex II; EN 1186-1Overall migration 10 mg/dm²; SML per Annex I
    FDA 21 CFR 177.1520USA polyolefin food contact21 CFR 176.170 table 2Conditions of use A–H; food types and temperatures
    GB 4806.7-2023China food contact plasticsGB 31604.1; GB 31604.8Total migration 10 mg/dm²; KMnO₄ consumption 10 mg/kg
    REACH Regulation (EC) No 1907/2006EU chemical safetyAnnex XVII; Article 33SVHC communication above 0.1 wt%

    What Drives Cold Cup Rim Rigidity at Wall Thickness Below 0.45 mm?

    The lower rim stack of a disposable cold cup typically collapses or ovalizes when the injection-molded sidewall lacks sufficient hoop rigidity at a thickness of 0.35–0.50 mm; a top-load ring crush test at 4°C commonly shows failure below 50 N on unreinforced thin-wall structures. In cold-fill beverage cups for iced tea, carbonated soft drinks, and portion cups, the applicable compliance set includes FDA 21 CFR 177.1520 for the resin, EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm², and EN 1186-1 for overall migration test design. The formulation blends 85–95 wt% M600X with 5–15 wt% random copolymer PP to improve low-temperature crack resistance; a sorbitol-based clarifying nucleator is added at 0.05–0.2 wt% and a blue toner masterbatch at 0.3–0.8 wt% to control yellowness. Production equipment is configured as stack molds with valve-gated hot runners and cone-shaped sprues, with a nozzle melt temperature of 235–255°C, a mold temperature of 12–30°C, an injection velocity of 300–600 mm/s, and a packing pressure of 35–55 MPa; cooling time is constrained to 3–5 s. The primary processing conflict is gate freeze time: at 0.35 mm wall thickness, the gate can freeze in 0.2–0.5 s, cutting off packing before sink and warpage are compensated, while increasing melt temperature above 270°C accelerates chain scission and generates off-odor defects and yellowing in the cup sidewall. Neat M600X may exhibit brittle failure below -20°C; freezer or ice-beverage cups require impact modification and validation under drop-test conditions. Terminal products include 200–500 mL conical drinking cups, 4–16 oz portion cups, and cold-brew cups with embossed fill lines.

    Typical thin-wall injection molding window by wall thickness for M600X
    Parameter0.35 mm wall0.80 mm wall
    Melt temperature at nozzle235–255°C225–245°C
    Mold temperature15–30°C20–40°C
    Injection speed300–600 mm/s200–400 mm/s
    Packing pressure35–55 MPa35–50 MPa
    Gate freeze time0.2–0.5 s0.8–1.5 s
    Cooling time3–5 s6–12 s

    In thin-wall lid molds with a valve-gated hot runner and a diaphragm gate at the tear tab, polypropylene M600X is run in 32- to 64-cavity tools at a melt temperature of 220–245°C and a mold temperature of 20–35°C. The lid geometry demands flatness of ≤0.3 mm across an 80 mm diameter when measured on a granite surface plate with a dial indicator, and a snap-fit inner ring that retains sealing force against a cup bead. Compliance for hot beverage lids includes EU Regulation (EU) No 10/2011, FDA 21 CFR 177.1520, and, where colored masterbatch is used, REACH Article 33 communication obligations if substances of very high concern exceed 0.1 wt%. The formulation uses 100 parts M600X with 0.5–1.5 phr slip masterbatch, 0.05–0.2 phr nucleating agent, and 1–2 phr color concentrate; for white lids, titanium dioxide masterbatch is added at 1.5–3.0 phr. The downstream process requires high-speed screw recovery with a back pressure of 5–10 MPa, injection velocity of 250–450 mm/s, and a holding time of 0.3–1.0 s; the screw velocity profile is programmed to drop to 80–120 mm/s only in the final 10–15% of fill to suppress jetting at the diaphragm gate. Main failure modes are tear-tab stress whitening and lid dome flattening after stacking; raising mold temperature above 35°C increases cycle time without improving flatness in high-speed tools. Terminal products include 80–110 mm lids for hot cups, cold cup flat lids, and overcap plugs used on dairy drink bottles.

    When a Ready-Meal Tray Requires Hot-Fill and Microwave Dual Resistance

    When a ready-meal tray must survive both a hot-fill step at 85–95°C and reheating in a 900 W microwave oven with hot spots reaching 110–130°C, the selection of M600X as the base resin requires distinct compliance and formulation decisions. The applicable food-contact compliance set includes EU Regulation (EU) No 10/2011 Annex IV sensory testing for organoleptic transfer, FDA 21 CFR 177.1520 for polyolefin microwavable trays, and China GB 4806.7-2023 total migration and potassium permanganate consumption limits. The formulation comprises 100 parts M600X with 0.1–0.3 phr primary antioxidant, 0.1–0.3 phr secondary antioxidant, 0.2–0.8 phr nucleating agent, and where opacity is required, 1.5–3.0 phr white masterbatch; black or colored trays add 1–2 phr color concentrate. The downstream injection molding process uses a melt temperature of 230–250°C, a mold temperature of 25–45°C, and a packing pressure of 40–60 MPa because the tray base must be packed through a long flow path of 150–250 mm at a nominal wall of 0.7–1.0 mm. The critical processing conflicts are hot-fill dimpling and warpage after microwave reheating; mold filling analysis and production-scale trials indicate that packing time must be extended to 1.5–3.0 s and cooling time held at 6–12 s to suppress post-mold distortion. Neat M600X should not be used for continuous exposure above 130°C, and trays requiring convection oven use above that limit are outside the grade's operational envelope. Terminal products include 300–1000 mL microwavable ready-meal trays, hot-fill condiment trays, and compartment trays with lidding film seals.

    Converters running stack molds for clear or translucent storage boxes observe that M600X thin-wall injection grade provides the required flow length for lids and bases up to 400 mm long at wall thicknesses of 0.6–0.9 mm, but the limiting variable is scratch resistance and stacking lug toughness rather than melt flow. The compliance set for household storage containers includes EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520 where food contact is claimed, and REACH Annex XVII for restricted substances in consumer articles; children's toys or childcare articles are outside this application unless explicitly tested under EN 71-3. The formulation uses 100 parts M600X with 0.1–0.3 phr nucleating agent, 0.5–2.0 phr antiblock masterbatch, and, when impact at -10°C is specified, 5–10 wt% impact copolymer PP replaces part of the M600X fraction. On the production floor, materials are processed at a melt temperature of 220–245°C, a mold temperature of 20–40°C, an injection speed of 200–400 mm/s, and a holding pressure of 35–50 MPa. The main ejector-stage failure modes observed in multi-cavity tools are distorted lids at the living hinge, sink marks above 0.02 mm on the lid surface measured by surface profilometer, and stress whitening at snap corners; these are addressed by profiling holding pressure to drop from 50 MPa to 20 MPa over 1.2 s and by raising mold temperature at the hinge region through conformal cooling. Terminal products include stackable storage boxes with capacities of 2–15 L, archive boxes, and under-bed containers.

    Cutlery Gate Freeze and Living-Hinge-Free Spork Configuration Limits

    Disposable cutlery lines operating at 12–24 cavities demand that the melt fill a narrow gateway of 0.8–1.2 mm across fork tines at the same time that the handle maintains a wall thickness of 1.2–1.8 mm. For polypropylene cutlery, the mandatory compliance set includes EU Regulation (EU) No 10/2011 for overall migration, FDA 21 CFR 177.1520 for the resin, and GB 4806.7-2023 for total migration; quick-service restaurant suppliers also apply brand-specific sensory protocols and REACH candidate list screening. The formulation uses 100 parts M600X with 0.1–0.2 phr nucleating agent, 0.3–0.8 phr slip masterbatch to reduce part sticking, and 1–2 phr white or colored masterbatch; for high-gloss black disposable forks, carbon black masterbatch is added at 0.5–1.5 phr. Processing on high-speed injection molding machines uses a barrel profile of 210–245°C, a nozzle melt temperature of 235–250°C, a mold temperature of 15–30°C, an injection velocity of 300–600 mm/s, and a holding pressure of 40–60 MPa. The principal processing limits are gate freeze at the tine subsprue and brittleness at the tine roots; if the gate freeze occurs before 0.4 s, the pack phase cannot densify the tine tips, leading to tine bending failure below 0.5 N when tested on a cantilever bend fixture. Terminal products include disposable forks, knives, spoons, spork combinations, and cake forks with lengths between 160–200 mm.

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    Certification & Compliance
    More Introduction

    Polypropylene Thin-wall Injection Grade PP M600X is supplied as a controlled-rheology, pelletised polypropylene formulated for high-speed injection moulding of thin-wall articles. The M600-series designation within the producer’s high-flow portfolio is associated with a nominal melt flow rate of 60 g/10 min when evaluated under ISO 1133-1:2022 at 230 °C and 2.16 kg. The X suffix identifies a stabilised nucleation or controlled-rheology package that reduces crystallisation time and improves dimensional consistency in rapid-cycle tools. Representative mechanical data generated on ISO 294-1 injection-moulded plaques and conditioned to ISO 291 at 23 °C and 50 % relative humidity include tensile yield stress of 34–37 MPa by ISO 527-2, flexural modulus of 1,500–1,700 MPa by ISO 178, notched Charpy impact strength of 2.0–3.0 kJ/m² by ISO 179-1/1eA, and heat deflection temperature B of 85–95 °C under 0.45 MPa by ISO 75-2/B. Density is typically 0.900–0.915 g/cm³ by ISO 1183-1. These values are data-sheet representations and not dual specification limits; lot-specific certificates of analysis remain the release reference.

    Table 1. Representative physical properties for PP M600X thin-wall injection moulding grade
    PropertyTest methodTypical value
    Melt flow rate, 230 °C/2.16 kgISO 1133-1:202260 g/10 min
    DensityISO 1183-10.900–0.915 g/cm³
    Tensile yield stressISO 527-2, 50 mm/min34–37 MPa
    Tensile yield strainISO 527-2, 50 mm/min6–8 %
    Flexural modulusISO 178, 2 mm/min1,500–1,700 MPa
    Notched Charpy impact, 23 °CISO 179-1/1eA2.0–3.0 kJ/m²
    Heat deflection temperature B, 0.45 MPaISO 75-2/B85–95 °C
    Water absorption, 23 °C, 24 hISO 620.01–0.03 %

    What Distinguishes PP M600X from Standard Injection Moulding Polypropylene Grades?

    The principal technical difference is flow length at low wall thickness. A conventional PP homopolymer with a melt flow rate of 12 g/10 min typically requires a practical minimum wall thickness above 0.70 mm for stable multi-cavity filling under ordinary hot-runner conditions, whereas PP M600X is applied in production at wall thicknesses from 0.35 mm to 0.65 mm. The higher melt-flow index does not automatically produce equal mechanical performance; the controlled-rheology package in the X designation is significant because it offsets part of the stiffness loss associated with high-flow grades. The result is a balance between flexural modulus, melt fluidity, and cycle time that is different from simple vis-broken polypropylene, which often shows lower notched impact strength and wider shrinkage anisotropy.

    Compared with a lower-flow PP homopolymer, M600X also shifts the processing boundary for gate freeze and packing. The high melt-flow grade reaches cavity filling more quickly, but the narrower gate-seal window requires more precise transfer from velocity-controlled filling to pressure-controlled holding. The nucleation package raises crystallisation temperature and shortens the cooling phase; in water-cooled tools with mould temperature of 40 °C, cycle-time reductions of approximately 15–25 % are reported in technical literature for thin-wall containers of 0.50 mm nominal wall compared with non-nucleated high-flow homopolymer. Published data for this specific configuration is limited, and tool geometry remains the controlling variable.

    Table 2. Differentiation against lower-flow PP homopolymer and impact copolymer in thin-wall injection
    AttributePP M600XPP homopolymer MFR 12PP impact copolymer MFR 25
    Melt flow rate60 g/10 min12 g/10 min25 g/10 min
    Practical minimum wall thickness0.35 mm0.70 mm0.50 mm
    Flexural modulus1,500–1,700 MPa1,450–1,650 MPa1,000–1,200 MPa
    Notched Charpy impact, 23 °C2.0–3.0 kJ/m²3.0–4.0 kJ/m²7.0–10.0 kJ/m²
    Typical application temperature range0–90 °C0–95 °C-20 to 80 °C
    Relative cycle-time index at 0.50 mm wall1.01.251.15

    The above comparative data are representative injection-moulded values drawn from supplier technical literature for thin-wall food-packaging polypropylenes; they are not specification limits. The impact copolymer offers substantially greater low-temperature toughness, but at a penalty of lower stiffness and higher haze. A random copolymer offers better contact clarity but lower heat deflection temperature and modulus, making it less suitable for stackable thin-wall containers subjected to warm filling above 60 °C.

    Primary use of PP M600X is in high-cavitation food-contact and packaging applications: dairy tubs, margarine containers, vending cups, thin-wall lids, and disposable housewares. In these applications, wall thickness is typically specified at 0.35–0.65 mm, and filled weight is reduced by approximately 10–20 % compared with conventional PP homopolymer because the higher melt flow allows thinner nominal sections without increasing injection pressure beyond 80 MPa in hot-runner tools. The grade is also applied to caps and closures where high filling speed and short hold time are required. The flexural modulus range of 1,500–1,700 MPa supports stacking strength in cylindrical cups, while the narrow shrinkage range reduces ovality in round containers. The nucleation package also yields lower surface haze than non-nucleated high-flow homopolymer, but PP M600X is not an optical clarity grade when compared with random copolymers used for transparent thin-wall cups.

    When Thin-Wall Moulding Demands Flow-Length Ratios Above 400:1

    Processing recommendations for PP M600X assume a reciprocating single-screw injection unit with a screw L/D ratio of 20:1–24:1 and a compression ratio of 2.0:1–2.5:1. Barrel temperature profiles from rear to nozzle are normally set at 190–210 °C, 210–220 °C, 220–240 °C, and 230–250 °C. Melt temperature measured by air shot should be maintained at 230–250 °C. Temperatures above 260 °C can initiate thermo-oxidative degradation, causing yellowing and a drop in notched impact strength, while temperatures below 220 °C reduce fluidity enough to compromise thin-wall filling.

    For wall thicknesses of 0.50 mm and flow-length ratios above 400:1, injection speed is normally set at 200–350 mm/s. For sections below 0.40 mm, screw-forward velocity may be raised to 350–400 mm/s to avoid premature freeze-off in the gate area. Holding pressure is typically 30–40 MPa, with hold time limited to gate freeze plus 0.2–0.5 s. Excessive hold time does not reduce sink marks in highly constrained thin sections; instead, it increases cavity-pressure decay time and can extend cycle time without improving part weight stability. Back pressure of 5–10 MPa and screw speed of 80–120 min⁻¹ are suitable starting points for uniform melt homogeneity without excessive shear heating.

    Mould temperature is normally maintained at 20–40 °C. Raising mould temperature to 50 °C improves surface gloss and reduces flow marks but extends cooling time. In high-cavitation stack tools, water manifold balancing and individual cavity temperature control are more critical than bulk mould setting because cavity-to-cavity temperature variation above 5 °C can produce measurable variation in post-mould shrinkage and part weight. Hot-runner manifold temperature is normally 230–240 °C, with valve-gate tips held at 240–250 °C to prevent stringing and gate freeze-off. Gate diameter for thin-wall packaging is typically 0.8–1.5 mm for direct edge gates or 1.2–2.0 mm for pin-point gates, depending on flow length and wall section.

    Because polypropylene does not hydrolyse, pre-drying of PP M600X is normally unnecessary when the resin is stored in sealed containers. If surface splay appears after storage at relative humidity above 60 %, drying for 2–3 h at 80 °C in a desiccant dryer is sufficient. The grade should not be blended with high-molecular-weight polyethylene carriers or low-flow colour masterbatch at high let-down ratios; such additions can introduce localised viscosity heterogeneity and gate hesitation. A high-flow PP-carrier masterbatch at 2–4 % let-down is preferable for colouring thin-wall parts without destroying the melt-flow balance. Machine check-ring wear, feed-throat temperature, and screw-recovery time are the principal batch-to-batch processing variables observed on production lines; screw-recovery time should remain below the cooling time to avoid limiting the cycle.

    An operational boundary emerges in tools with wall thickness below 0.35 mm. At such dimensions, apparent shear rate in the gate can exceed 100,000 s⁻¹, and filling becomes highly sensitive to melt-temperature variation and check-ring leakage. Short shots, flow marks, and burned surfaces from air entrapment are more common in this range. The material may be used, but tool validation must include cavity-pressure transducers and short-shot studies to establish a repeatable transfer point. For applications requiring notched Charpy impact above 5.0 kJ/m² at -20 °C, PP M600X is not the appropriate selection; impact copolymers or blends should be considered.

    From a regulatory standpoint, PP M600X in food-contact packaging should be used only with lot-specific confirmation that the base resin and additive package comply with FDA 21 CFR 177.1520 for olefin polymers and EU 10/2011 where applicable. The producer’s safety data sheet should be checked for REACH SVHC status and RoHS 2011/65/EU heavy-metal declarations. Because the exact additive package may not be disclosed in standard technical literature, published data for this specific configuration is limited; compliance for end-use articles is the responsibility of the converter and requires migration testing under EN 1186 or EU 10/2011 simulant protocols. Avoid storage of finished parts at temperatures above 90 °C for extended periods unless application-specific heat-ageing data are available. The grade is generally unsuitable for continuous use in contact with strong oxidising acids, chlorinated solvents, or high-purity aromatic hydrocarbons without chemical resistance verification.