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MOSTEN PP Homopolymer MT 825

    • Product Name: MOSTEN PP Homopolymer MT 825
    • 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 104983
    Material MOSTEN PP Homopolymer MT 825
    Polymer Type Polypropylene Homopolymer
    Melt Flow Rate 230 C 2 16 Kg 8 g/10 min
    Density 0.905 g/cm³
    Tensile Strength At Yield 34 MPa
    Elongation At Yield 10 %
    Flexural Modulus 1500 MPa
    Izod Impact Strength Notched 23 C 4 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 90 °C
    Vicat Softening Temperature A 10 N 155 °C
    Melting Point 165 °C
    Rockwell Hardness R95

    As an accredited MOSTEN PP Homopolymer MT 825 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing MOSTEN PP Homopolymer MT 825 is supplied in 25 kg polyethylene-lined paper bags, palletized and shrink-wrapped for safe transport.
    Container Loading (20′ FCL) 20′ FCL: Polypropylene homopolymer pellets in 25kg bags, palletized, shrink-wrapped, secured to prevent shifting, moisture-protected.
    Shipping MOSTEN PP Homopolymer MT 825 is shipped as non-hazardous polymer pellets in sealed moisture-proof bags or bulk containers. Keep dry, away from heat and direct sunlight. Avoid dust accumulation; use grounded equipment during transfer. Standard dry cargo transport is suitable under clean, ventilated conditions.
    Storage Store MOSTEN PP Homopolymer MT 825 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 buildup. Avoid contact with strong oxidizers. Ensure proper grounding and good housekeeping to minimize static and fire hazards.
    Shelf Life Shelf life is typically 2 years from manufacture when stored in original, unopened packaging in dry, cool conditions.
    Application of MOSTEN PP Homopolymer MT 825

    Thin-Wall Injection Moulding of Dairy and Convenience-Food Containers

    In high-cavitation stack-mould production of dairy tubs with wall stock between 0.45 mm and 0.80 mm, the 25 g/10 min melt-flow rate of MT 825 measured at 230 °C under 2.16 kg load in accordance with ISO 1133-1:2022 establishes the pressure-drop window and gate-freeze behaviour that separate a commercially viable cycle time from a blocked cavity pack. On rotary stack moulds with 2 × 8 or 2 × 16 cavity arrays, the material is injected at melt temperatures of 230–250 °C through valve-gate drops of 0.8–1.2 mm into moulds held at 10–30 °C; the low mould temperature accelerates skin solidification but increases in-cavity shear stress, which is controlled by limiting injection velocity to 0.25–0.60 m/s and maintaining holding pressure between 60 MPa and 90 MPa until gate seal. Flow length-to-wall ratios of 150:1 to 200:1 are achievable without flash only when the hot-runner manifold is zoned to maintain melt-temperature deviation below ±2.5 °C and the clamp force available at projected-area pressure of 40–60 MPa is not exceeded. Pre-drying in a desiccant dryer at 80 °C for 2.0–3.0 h is required if moisture content exceeds 0.05% by weight, for example after outdoor storage at relative humidity above 60%; excessive residual moisture produces surface streaks and reduction of interlayer adhesion in printed lids. The food-contact status of MT 825 is anchored to FDA 21 CFR 177.1520 and European Regulation EU 10/2011, with overall migration below 10 mg/dm² in aqueous and acidic simulants and with organoleptic neutrality in dairy fat simulants. Formulation practice for this homopolymer in thin-wall dairy packaging uses 100% virgin resin for natural translucent containers, 1.5–3.0 wt% titanium dioxide-containing white PP masterbatch for light-barrier tubs, and 1.0–2.0 wt% colour concentrate with PP carrier when brand-matched lids are moulded; slip additives, if required for denesting, are restricted to 0.10–0.20 wt% erucamide because higher loadings add migration burden and reduce sidewall print adhesion. Terminal product types include round dairy cups, rectangular margarine tubs, cold-fill dessert containers, and snap-on overcaps.

    Control ParameterStandard/DesignationValue/Limit
    Melt-flow rateISO 1133-1:202225 g/10 min
    Food-contact resin statusFDA 21 CFR 177.1520Conformance as olefin polymer
    Overall migration in aqueous and acidic simulantsEU 10/201110 mg/dm²
    Residual moisture before mouldingDesiccant drying method≤0.05%

    Closure manufacturing on 64-cavity hot-runner platforms imposes a shear-history boundary on MT 825 that is not visible in standard ISO spiral-flow data. Valve-gate drops of 0.6–1.0 mm and shear rates above 10,000 s⁻¹ lower melt viscosity in the runner but can generate local temperature overshoot at the gate if fill speed is not matched to rheology; cavity-to-cavity shot-weight variation is maintained within ±0.03 g on production-scale lines only when barrel melt temperature is held at 235–255 °C and the hot-runner manifold is zoned to ±2.5 °C. The homopolymer is injected at velocities of 70–120 mm/s, with holding pressure between 40 MPa and 60 MPa and cooling time of 4.0–8.0 s, producing total cycle times of 7.5–12.0 s on 64-cavity moulds for flat-thread screw closures with wall thickness 0.7–1.2 mm. Formula adjustment for closure function is limited: erucamide slip additive at 0.10–0.20 wt% is added to achieve removal-torque reduction after 24–72 h of controlled migration, while loadings above 0.30 wt% cause plate-out on mould cores and intermittent torque failures due to surface bloom accumulation. Pigmentation is restricted to 1.0–2.0 wt% of PP-carrier colour masterbatch; inorganic pigments are preferred because certain organic chemistries can nucleate homopolymer crystallization and alter cap-diameter shrinkage by up to 0.2–0.4%. Compliance for food-contact closures is governed by FDA 21 CFR 177.1520 and EU 10/2011, with additional organoleptic testing for low-odour water and aseptic dairy applications. Terminal product types include screw caps for non-carbonated beverages, snap-over closures for nutrition powders, and dispensing plugs for condiment bottles; for carbonated beverages with dissolved CO₂ equilibrium pressure above 3.0 bar at 20 °C, MT 825 is not recommended because the homopolymer notched impact strength below 2.5 kJ/m² is insufficient for drop-load crack resistance, and an impact copolymer or tamper-evident laminate must be substituted.

    What Limits Homopolymer Use in Laboratory Consumables Subjected to Autoclave Cycling?

    Autoclave cycling at 121 °C and 0.10–0.12 MPa overpressure places thin-walled homopolymer PP in the upper tail of its heat-deflection range. For MT 825, Vicat B50 softening of approximately 88–92 °C under ISO 306 means that a microcentrifuge tube wall of 0.5 mm accumulates compressive creep under stacked load during the 15–20 min dwell, producing ovality and cap-seal failure after repeated cycles. The operational boundary is therefore explicit: laboratory disposables made from MT 825 are specified for non-autoclaved diagnostic workflows, for lots sterilized by ethylene oxide according to ISO 11135, or for gamma irradiation at validated doses not exceeding 25 kGy; repeated steam autoclave use is excluded from the design envelope. In cleanroom injection moulding, MT 825 is processed at melt temperatures of 220–240 °C and mould temperatures of 8–15 °C to minimize sink marks in pipette-tip cones with wall thickness down to 0.3 mm; valve-gated hot runners with gate diameters of 0.35–0.50 mm are used for tip filling, while microcentrifuge tube moulds use tunnel gates to avoid gate vestige on sealing surfaces. Formulation for analytical labware is 100% virgin resin with no external slip, erucamide, or migratory antistat in the default grade; if electrostatic discharge control is required for powder dosing, a non-migratory antistatic masterbatch at 0.2–0.5 wt% may be added only after the extractable profile is revalidated. Compliance is established through USP Class VI biological reactivity data, ISO 10993-5:2009 cytotoxicity evaluation, and manufacturing under ISO 13485:2016 cleanroom documentation; residual monomer and oligomer extractables are controlled under REACH Regulation 1907/2006. Published data for the creep-rupture behaviour of this specific homopolymer at autoclave dwell is limited, so repeated autoclave validation is required if any deviation from this boundary is considered. Terminal product types include pipette tips, reagent reservoirs, assay plates, and microcentrifuge tubes for non-thermal bioscience workflows.

    When Homopolymer Replaces Impact Copolymer in Small Appliance Non-Load-Bearing Parts

    The substitution boundary for MT 825 in small appliance components is defined by continuous service temperature below 80 °C and minimum impact energy above 1.0 kJ/m² at -20 °C, beyond which an impact copolymer or mineral-filled copolymer becomes necessary. Parts such as detergent drawer fronts, tumble dryer lint-filter frames, refrigerator air-duct baffles, and wire-management clips are injection moulded from MT 825 when UL 94 HB flame class is acceptable for the end-use and when no direct contact with current-carrying uninsulated terminals is specified in the appliance safety review. The melt is processed at 220–240 °C into moulds held at 30–50 °C to reproduce grained or matte surfaces without sink in ribs; gate sizing of 0.8 mm minimum is maintained for talc-loaded variants to avoid gate freeze and surface sharkskin on textured faces. For parts requiring higher flexural modulus and reduced heat sag, MT 825 is compounded on a corotating twin-screw extruder with L/D 40:1 at 210–230 °C with 10–20 wt% talc masterbatch, raising flexural modulus from approximately 1,500 MPa to 2,400–2,800 MPa and shifting the heat deflection temperature under 0.45 MPa load from 95 °C toward 110 °C. The talc modification, however, lowers notched impact strength and melt fluidity, so wall thickness below 1.2 mm should not be specified without flow simulation. Compliance is anchored to IEC 60335-1 for household-appliance safety, IEC 60695-2-12 glow-wire flammability index testing, UL 94 HB burn classification as specified by the end-product standard, RoHS Directive 2011/65/EU for homogeneous-material lead, mercury, and cadmium limits, and REACH Regulation 1907/2006 for SVHC disclosure. Published data for the glow-wire ignition temperature of this specific homopolymer is limited, so component-level verification on the actual wall thickness is required before series production. Terminal product types include appliance trim, air-directing baffles, detergent drawer fronts, and non-structural harness clips.

    Because EN 71-3 imposes an eight-metal migration limit on playable surfaces, household storage and organizational articles made from MT 825 require pigment selection that does not exceed specific migration limits under acidic sweat simulants. The homopolymer is moulded at 220–245 °C melt temperature and 15–30 °C mould temperature on stack-turn moulds for rectangular storage boxes with living hinges; 1.0–3.0 wt% PP-carrier colour masterbatch and 5.0–10.0 wt% talc masterbatch are added to reduce warpage in flat walls of 2.0–3.5 mm thickness, while antistatic masterbatch at 0.05–0.10 wt% is used only for dust-free storage articles because higher loadings reduce weld-line strength in stack-moulded corner bosses. Terminal products include modular storage boxes, drawer organizers, office trays, and children's storage bins; food-contact migration certification under EU 10/2011 is not granted by this formulation unless the selected pigments and talc are individually verified.

    Non-Returnable Crate Moulding Sits on a Narrow Impact Boundary at Freezing Temperatures

    On accumulator-assisted injection presses with clamp force from 1,300 t to 2,800 t, large-area transit packaging moulded from MT 825 is limited to non-returnable or short-rotation crates and totes because the homopolymer notched impact strength falls below practical handling thresholds when cold-room or outdoor winter temperatures drop below 0 °C. MT 825 is processed at melt temperatures of 230–250 °C and mould temperatures of 15–35 °C; cycle times for crates with wall thickness 3.0–6.0 mm typically range from 45 s to 90 s, with sequential valve-gate opening required to prevent knit lines at corner intersections. Formulation for outdoor stacking uses 2.0–5.0 wt% carbon black masterbatch for ultraviolet screening and 2.0–5.0 wt% mineral-filled masterbatch to reduce top-load creep; higher filler loadings are not used because thin ribs below 3.0 mm exhibit brittle failure at injection gates. REACH Regulation 1907/2006 and RoHS Directive 2011/65/EU apply to non-food industrial packaging, while food-contact migration certification is required only where crates contact unpackaged food. Terminal product types include stackable ambient-distribution produce crates, logistics trays, and non-food tote boxes.

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    Certification & Compliance
    More Introduction

    ORLEN Unipetrol RPA s.r.o. supplies MOSTEN PP Homopolymer MT 825 as a controlled-rheology polypropylene homopolymer in pellet form for injection moulding. The nominal melt mass-flow rate is 25 g/10 min at 230 °C under a 2.16 kg load, measured according to ISO 1133-1:2022. The density is 0.905 g/cm³ under ISO 1183-1. The intended application envelope covers rigid thin-wall packaging, caps and closures, housewares, and technical mouldings where low melt viscosity, high stiffness, and short cooling time control cycle economics. Because the polymer chain structure contains no ethylene comonomer, the moulded part is translucent rather than transparent and exhibits higher tensile modulus than a random copolymer at equivalent melt flow. Compared with impact copolymers, MT 825 has lower notched impact but better stiffness and lower tendency to surface marking at room-temperature service. Typical pellet bulk density is 0.52–0.56 g/cm³. The grade is not hygroscopic, and sealed storage at 10–40 °C with exclusion of direct UV exposure is normally sufficient.

    What Separates MT 825 from Low-Flow Homopolymer Grades?

    The main difference is melt viscosity during mould filling. At 25 g/10 min, MT 825 has a lower molecular weight than a general-purpose homopolymer with an MFR of 3 g/10 min. The practical result is lower injection pressure and shorter filling time in wall sections below 1.5 mm. On a single-cavity thin-wall container mould with a 1.2 mm side wall and a fan gate, peak injection pressure is reduced by approximately 30% compared with the 3 g/10 min grade at the same melt temperature and injection speed. The trade-off appears in fracture behaviour: MT 825 records Charpy notched impact near 2.5 kJ/m² at 23 °C under ISO 179-1/1eA, whereas a low-flow homopolymer may reach 4.0 kJ/m² or higher. The higher flow therefore reduces clamp force and improves thin-wall fill, but it imposes a property cliff in impact resistance.

    Comparative Property Profile of MT 825 and Reference Polypropylene Grades
    Property / MethodMOSTEN MT 825PP Homopolymer MFR 3 g/10 minPP Impact Copolymer MFR 25 g/10 min
    Melt mass-flow rate ISO 1133-1:202225 g/10 min3 g/10 min25 g/10 min
    Density ISO 1183-10.905 g/cm³0.905 g/cm³0.900 g/cm³
    Flexural modulus ISO 1781600 MPa1500 MPa1100 MPa
    Tensile stress at yield ISO 527-235 MPa34 MPa24 MPa
    Charpy notched impact ISO 179-1/1eA, 23 °C2.5 kJ/m²4.0 kJ/m²8.0 kJ/m²
    Vicat softening temperature A50 ISO 306154 °C155 °C140 °C

    The values are representative and must be checked against the production lot certificate of analysis. Replacing an impact-copolymer part with MT 825 can reduce room-temperature notched impact by more than 60%, while replacing a low-flow homopolymer with MT 825 improves flow length and lowers clamp force but sacrifices approximately 1.5 kJ/m² in Charpy notched impact.

    Processing Window and Screw Configuration

    The recommended melt-temperature range is 220–260 °C, with optimum injection-moulding results on production machinery generally observed at 230–250 °C. Nozzle temperatures below 210 °C can produce short shots in multi-cavity tools, while sustained melt temperatures above 270 °C accelerate thermo-oxidative degradation, causing yellowing and a loss of melt strength. A general-purpose polyolefin screw with 20:1 to 24:1 L/D and compression ratio of 2.5:1 to 3.5:1 is adequate for homogeneous melt preparation. The barrel profile from feed throat to nozzle is typically set at 210/220/230/240/240 °C. Back pressure is maintained at 0.5–1.0 MPa; higher back pressure increases shear heating and may degrade molecular weight. Mould temperature is normally maintained at 20–50 °C. Lower mould temperatures shorten cooling time but increase frozen-in orientation and may reduce practical impact resistance. Linear mould shrinkage is typically 1.0–1.5% under ISO 294-4, depending on wall thickness, gate location, and mould temperature.

    Regrind additions up to 25 wt% of clean, dry sprues and runners do not normally produce measurable changes in tensile stress at yield. On production lines, the limiting variable is not the base resin but contamination of regrind with paper labels, silicone release agents, or other polymers. If post-industrial regrind exceeds 30 wt%, melt-pressure variation during screw recovery increases because of non-uniform particle size and bulk density. The regrind should be dried for 2 h at 80 °C, and a screen pack should be used at the nozzle if contamination is suspected. Published data for this specific configuration is limited, so start-up trials should include a gate-freeze study and a 12-shot weight-stability check.

    When Thin-Wall Packaging Requires Melt Flow Rates Above 20 g/10 min

    Thin-wall packaging with wall thickness below 0.8 mm imposes a flow-length-to-wall-thickness ratio that low-flow grades cannot fill at practical clamp forces. MT 825 is placed in this processing envelope because the 25 g/10 min melt flow rate permits lower injection pressure in multi-cavity tools. In a 48-cavity round container mould with a cold runner, the observed clamp force requirement is approximately 20–25% lower than that of an MFR 12 g/10 min homopolymer at the same shot size and cycle time. The grade is not suited to deep-draw thermoforming because controlled-rheology modification reduces melt strength and increases sag during radiant heating; a high-melt-strength polypropylene should be selected for that process. In caps and closures, the low viscosity supports filling of fine threads and tamper-evident bands, but stress-crack resistance with aggressive detergents must be evaluated under ISO 22088-2 or an equivalent method because homopolymer polypropylene can fail at low strains when exposed to surface-active agents.

    The short-term heat resistance of the homopolymer structure is expressed by a Vicat softening temperature A50 of 154 °C under ISO 306 and a heat deflection temperature of 95 °C at 0.45 MPa under ISO 75-2. The flexural modulus of 1600 MPa under ISO 178 is above impact-copolymer values and slightly above low-flow homopolymer values. Tensile stress at yield is 35 MPa under ISO 527-2, with tensile strain at yield near 9%. Charpy notched impact at 23 °C is 2.5 kJ/m²; at 0 °C the value drops sharply, which limits unsupervised impact loading in cold-chain distribution. Electrical properties are typical of unfilled polypropylene homopolymer: volume resistivity above 10¹⁴ Ω·m under IEC 62631-3-1, and comparative tracking index above 600 V under IEC 60112. These electrical values are general homopolymer characteristics rather than grade-specific design data.

    Regulatory Status and Food-Contact Documentation Must Be Verified per Lot

    Compliance and Migration Test Matrix
    Regulation / StandardMethod or ClauseCondition
    EU 10/2011 food contactOverall migration10 mg/dm² for plastic food-contact articles
    FDA 21 CFR 177.1520Olefin polymersConditions A–H depending on food type
    REACH SVHCArticle 330.1% w/w declaration threshold
    RoHS 2011/65/EUPb, Cd, Cr(VI), Hg, PBB, PBDE1000 mg/kg for Pb/Hg/Cr(VI), 100 mg/kg for Cd

    Food-contact declarations are formulation-specific. Colour masterbatch, processing aids, or external mould release agents may change the migration profile of the finished article. The converter must therefore perform end-article verification under EU 10/2011 and FDA 21 CFR 177.1520 rather than relying solely on the resin certificate.

    Where optical clarity or hot-seal strength is required, MT 825 is normally replaced by a random copolymer with ethylene content near 2–4 wt%. The random copolymer has lower haze, lower Vicat softening temperature, and a seal initiation temperature below 125 °C, while the homopolymer seals only near its melting range. MT 825 cannot provide transparent retort containers or film-grade seal layers. For living-hinge applications, a lower-flow homopolymer is often preferred because controlled-rheology high-flow grades may show earlier hinge whitening after repeated flexing; published data for MT 825 in living hinges is limited.

    On a production-scale thin-wall container line using a 2500 kN injection moulding machine and a 2+2 stack mould, the material is typically processed at a melt temperature of 235 °C and mould temperature of 35 °C. Screw recovery time remains stable when pellet bulk density is held within 0.52–0.56 g/cm³; batch-to-batch pellet geometry variations can alter shot weight by 0.5–1.0%. Gate freeze-off time in a 0.9 mm side-wall dairy cup is typically 0.8–1.2 s, and ejection is initiated when the part surface temperature reaches approximately 80 °C to limit distortion. Under these conditions, cycle time is controlled by cooling rather than by material viscosity. Substitution into a cap mould designed for MFR 12 g/10 min requires verification of check-ring performance and nozzle shut-off repeatability because the lower melt viscosity increases the risk of drool and reduces cushion repeatability. If the non-return valve is worn, shot-to-shot variation may exceed 0.15% and cause dimensional drift in the tamper-evident band.

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