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Indian Oil PP Homopolymer 1030FG

    • Product Name: Indian Oil PP Homopolymer 1030FG
    • 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 956500
    Melt Flow Index 230 C 2 16 Kg 3.0 g/10 min
    Density 0.905 g/cm³
    Tensile Strength At Yield 33 MPa
    Elongation At Yield 12 %
    Flexural Modulus 1350 MPa
    Izod Impact Strength Notched 23 C 4.0 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 100 °C
    Vicat Softening Point 155 °C
    Melting Point 165 °C
    Rockwell Hardness R95

    As an accredited Indian Oil PP Homopolymer 1030FG factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in 25 kg woven polypropylene bags with moisture barrier lining, ensuring safe handling and storage.
    Container Loading (20′ FCL) 20′ FCL container loading of Indian Oil PP Homopolymer 1030FG ensures safe, dry, contamination-free packing of polymer granules for transport.
    Shipping Shipping description: Polypropylene Homopolymer, Indian Oil 1030FG. Non-hazardous, not regulated per IMDG/ADR/IATA; no UN number required. Supplied as virgin granules in 25 kg bags, shrink-wrapped on pallets. Protect from moisture, heat, and prolonged sunlight during transit. Keep dry and away from ignition sources.
    Storage Store Indian Oil PP Homopolymer 1030FG in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and ignition sources. Keep packaging sealed to prevent moisture absorption and contamination. Avoid prolonged UV exposure, and store away from strong oxidizers. Maintain stable temperatures, and use within the recommended shelf life for optimal performance.
    Shelf Life Shelf life is typically 12 months if stored in original, unopened packaging away from heat, moisture, and direct sunlight.
    Application of Indian Oil PP Homopolymer 1030FG

    For thin-wall injection-moulded dairy and delicatessen containers, Indian Oil PP Homopolymer 1030FG is processed at a melt temperature of 210°C to 230°C with a nominal melt flow rate of 10 g/10 min at 230°C under 2.16 kg load per ISO 1133-1:2022, permitting flow lengths adequate for wall sections from 0.45 mm to 0.80 mm in multicavity stack tools. Regulatory compliance for this application category is established under EU No 10/2011 with an overall migration limit of 10 mg/dm², FDA 21 CFR 177.1520 for olefin polymers in contact with aqueous and fatty foods, and Indian IS 10910 for food-grade polypropylene. Formulation adjustment on the converting line consists of colour masterbatch metered at 1.0 wt% to 2.0 wt% and, where interlayer denesting force reduction is critical, erucamide-based slip concentrate is added at 0.5 wt% to 1.5 wt%; all slip additives must be listed in the positive lists of the relevant food-contact regulation before use. The downstream process employs accumulator-assisted injection moulding machines with clamp force between 1,500 kN and 3,500 kN, a single-flight barrier screw of L/D 20:1 to 24:1, injection velocities of 300 mm/s to 600 mm/s, mould temperature from 10°C to 30°C, and hold pressure between 40 MPa and 60 MPa. On such lines, gate freeze time rather than fill time limits cycle length; processing records from 32-cavity thin-wall tools show that hold pressures above 45 MPa without valve-gate pin retraction can produce gate vestige tearing when mould temperature falls below 15°C. Terminal products include dairy tubs, delicatessen containers, cold-food meal trays, and disposable food-service cups, provided that hot-fill conditions do not exceed 80°C for continuous service.

    What Injection Moulding Parameters Govern Torque Retention in PP Homopolymer Closures?

    Closure moulding with 1030FG requires differentiation from impact-copolymer PP because the homopolymer matrix exhibits lower environmental stress cracking resistance in contact with polar oils and aggressive surfactant systems, making additive selection the dominant variable for long-term sealing reliability. The applicable compliance set includes FDA 21 CFR 177.1520 for olefin polymers, EU No 10/2011 for food-contact plastics, and EN 71-3 where coloured closures are sourced for child-accessible packaging, although the latter is a toy-safety standard and applies only when marketing use crosses into juvenile products. At the compounding or masterbatch dosing stage, torque-reducing slip masterbatch is metered at 0.8 wt% to 1.5 wt% to achieve a coefficient of friction of 0.20 to 0.35 under ISO 8295; pigment loading is maintained below 1.5 wt% because higher pigment concentrations act as nucleating impurities, altering non-isothermal crystallisation and increasing cap diameter shrinkage beyond 1.5%. Downstream production runs use hot-runner stack moulds with thermal gate tips controlled to ±5°C of the melt set point, a melt temperature of 220°C to 240°C, injection velocity of 40 mm/s to 80 mm/s for wall sections from 1.0 mm to 1.8 mm, holding pressure of 50 MPa to 65 MPa, and mould temperature of 15°C to 25°C. Ejection torque on some 24-cavity closure tools rises when gate vestige height exceeds 0.15 mm; this is managed by reducing hold-pressure duration rather than increasing mould cooling. Terminal types include screw caps for edible oil bottles, condiment flip-top overclosures, spice jar caps, and tamper-evident band closures. Published long-term stress crack data for 1030FG in contact with high-oleic edible oil at temperatures above 40°C is limited, so compatibility testing under ASTM D1693 is required before substituting into aggressive oxygenated or high-alcohol formulations above 20 vol%.

    Where melt flow and food-contact conformity are required in thicker-section housewares, 1030FG is run at lower screw speeds and longer holding profiles than thin-wall packaging because the homopolymer is more prone to sink mark formation over ribs with section ratios greater than 1.5:1. The relevant regulatory framework is EU No 10/2011 with Articles 15 and 17 documentation obligations, FDA 21 CFR 177.1520, REACH EC 1907/2006 for SVHC and substance restrictions, and RoHS 2011/65/EU where the articles contain electrical accessories such as built-in LED partitions. Formulation addition on conversion lines includes clarifier masterbatch at 0.25 wt% to 0.50 wt% for transparent storage containers and antistatic masterbatch at 0.5 wt% to 1.0 wt% for dust-sensitive utility organisers; mineral filler masterbatches are avoided because they depress the melt flow rate and reduce the food-contact clarity required in this segment. The downstream process uses standard hydraulic injection moulding machines with clamp force from 1,000 kN to 2,500 kN, screw L/D of 20:1 to 22:1, melt temperature between 200°C and 220°C, mould temperature from 20°C to 40°C, and a cushion held at 3 mm to 5 mm to ensure packing linearity. In production of long flat lids, warpage measured across the diagonal exceeds 2.0 mm when post-mould cooling jigs are omitted; controlled cooling at 25°C for 30 s to 60 s reduces dimensional deviation to below 1.0 mm. Terminal products include reusable lunch boxes, kitchen drawer organisers, dry food storage containers, and utility baskets for pantry use, with an operational temperature ceiling of 80°C unless microwave heating is separately validated under the final article's full migration testing program.

    Heat Deflection and Shrinkage Control in Refrigerator Interior Components

    Moulded refrigerator door racks, egg trays, and detergent dispenser housings use 1030FG because the grade's heat deflection temperature under 0.45 MPa is typically 95°C per ISO 75-2, providing dimensional stability at service temperatures up to 60°C inside refrigeration and dishwashing machine peripheral zones. Compliance for these non-food-contact but household-grade articles is anchored to IEC 60335-1 for mechanical and thermal safety of household appliances, UL 94 HB for slow-burning classification under UL 94, REACH EC 1907/2006, and RoHS 2011/65/EU. The polymer contributes a flexural modulus of 1,450 MPa per ISO 178 and linear mould shrinkage of 1.2% to 1.6% per ISO 294-4, while tensile yield stress of 34 MPa under ISO 527-2 supplies the short-term load resistance required for snap-fit assembly. At the formulation stage, nucleating masterbatch is dosed at 0.10 wt% to 0.25 wt% active content to elevate crystallisation onset temperature by approximately 5°C and reduce post-mould shrinkage anisotropy between flow and cross-flow directions; colour masterbatch is metered at 1.0 wt% to 2.0 wt%, but high-aspect-ratio pigments are excluded where sink mark control is critical. The downstream process uses medium injection velocity of 50 mm/s to 100 mm/s, melt temperature from 210°C to 230°C, mould temperature of 20°C to 30°C, and two-stage holding pressure at 40 MPa for 4 s followed by 25 MPa for 8 s; cooling time ranges from 15 s to 25 s. In field trials on detergent dispenser housings with thick bosses behind snap-fit lugs, sink marks above 0.05 mm depth occur when the boss-to-nominal wall ratio exceeds 2.0:1; this is mitigated by gas-counterpressure or by reducing hold pressure and accepting longer cycle time. Terminal products include refrigerator door racks, egg trays, washing machine detergent dispenser housings, and vacuum cleaner attachment brackets, excluding any component exposed to continuous service above 80°C or to hot alkaline wash liquors at pH above 10.5 without performance testing.

    Unlike impact-copolymer PP grades specified for refrigerated distribution crates, 1030FG is reserved for large dry food ingredient pails and dry-goods transport containers where the operating temperature remains above 0°C and impact loading is limited to stacking and moderate handling. Regulatory requirements for this segment include EU No 10/2011 for dry and aqueous food contact, FDA 21 CFR 177.1520, and IS 10910 for packaging materials marketed in India; where pails are intended for export, the manufacturer's Declaration of Compliance must state that the food-contact layer contains no intentionally added bisphenol A or phthalates. Formulation adjustment for outdoor warehouse use comprises UV stabiliser masterbatch at 0.5 wt% to 1.5 wt% and a blue-violet tint masterbatch at 0.01 wt% to 0.05 wt% to mask light-induced yellowing; lubricant masterbatch is added at 0.2 wt% to 0.5 wt% where ejection of deep pails produces drag marks. Downstream production uses injection moulding machines with clamp force from 4,000 kN to 8,000 kN, melt temperature of 210°C to 230°C, mould temperature from 20°C to 40°C, and two-stage packing profiles of 50 MPa for 5 s and 35 MPa for 10 s to compensate for volumetric shrinkage in walls of 3.0 mm to 5.0 mm; total cooling time is 25 s to 40 s. In deep-draw pails, demoulding vacuum is applied when cavity pressure at gate freeze exceeds 30 MPa, because early ejection otherwise distorts the rim diameter beyond the ±0.8 mm tolerance required for snap-on lids. Terminal products include stackable dry food ingredient pails, spice transfer bins, bulk sachet handling containers, and reusable dry fruit storage pails with tamper-evident seal ledges.

    When Food-Grade PP is Used for Educational Stationery Components

    Stationery components manufactured from 1030FG include ruler bodies, desk trays, ring binder covers, and pencil case shells where food-grade resin status reduces regulatory complexity under REACH Annex XVII restrictions and EN 71-3 migration limits for colourants and heavy metals when the article is classified as a toy-adjacent school product. The compliance profile is less demanding than food-contact packaging, but RoHS 2011/65/EU remains applicable for electronic accessories such as smartpen housings or LED-equipped organisers. Formulation addition on the conversion line is limited to colour masterbatch at 1.0 wt% to 2.0 wt%; no impact modifier is added, and external mould release, when required, is applied at a dilution of 1:100 to 1:200 rather than melt compounded. The downstream process runs on standard reciprocating-screw injection machines with shot weights from 50 g to 200 g, melt temperature of 190°C to 210°C, mould temperature of 15°C to 25°C, and wall thickness from 1.5 mm to 2.5 mm; short shots at the tip of ruler scales occur when injection velocity is held below 30 mm/s, so velocity is raised to 60 mm/s for crystallisation-sensitive features. Terminal products are limited to educational stationery and desktop organisation articles; load-bearing hinges and snap-fits subject to repeated flexure beyond 90° are not specified in 1030FG because homopolymer fatigue resistance is lower than impact-copolymer PP.

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    Certification & Compliance
    More Introduction

    Indian Oil PP Homopolymer 1030FG is a general-purpose injection-moulding grade produced by Indian Oil Corporation Limited. The producer’s published datasheet positions the grade at a nominal melt mass-flow rate of 10.0 g/10 min measured at 230 °C under a 2.16 kg load in accordance with ISO 1133-1:2022. Density is reported at 0.90 g/cm³ under ISO 1183-1:2019, tensile stress at yield at 34 MPa under ISO 527-2:2012, flexural modulus at 1,500 MPa under ISO 178:2019, and notched Izod impact strength at 2.5 kJ/m² under ISO 180:2023. The FG suffix indicates a food-contact formulation intent, not a finished-article compliance certification. Typical applications include injection-moulded caps, closures, housewares, containers and thin-wall food-contact articles in which fast mould filling and adequate stiffness are required. The fused-ring structure and linear isotactic architecture provide high crystallinity and relatively low melt strength; consequently, the grade is suited to injection moulding but is not the primary choice for stretched-tape, raffia or deep-draw thermoforming operations where high melt strength is essential.

    The molecular weight distribution of this homopolymer class is narrow enough to produce stable melt viscosity during plastication, but the 10.0 g/10 min fluidity lowers viscous heating and shortens fill time. In multicavity tools this reduces peak hydraulic pressure and allows thinner wall sections, but it also narrows the processing window for screw-recovery repeatability because the low-viscosity melt is sensitive to back-pressure variation. The current certificate of analysis is the controlling document for any production batch; the values discussed here are representative of the producer’s published nominal profile and should not replace batch-specific data for tool design or regulatory submission.

    What Differentiates 1030FG Within the Indian Oil Homopolymer Portfolio?

    The principal distinction is melt-flow positioning. Lower-MFR homopolymer grades in the 2.0–3.5 g/10 min range are selected for stretched tapes, raffia and monofilament because their higher molecular weight contributes sufficient melt strength for draw ratios above 6:1. 1030FG sacrifices that stretch-orientation window for improved spiral-flow length and reduced injection pressure. Compared with an ethylene-propylene random copolymer containing 1.5–3.5 wt% ethylene, 1030FG exhibits higher tensile yield strength and flexural modulus, lower notched Izod impact, higher melting peak and reduced optical clarity. These differences make 1030FG preferable for rigid, dimensionally stable parts; random copolymers are generally selected for high-clarity containers, freezer applications and articles requiring toughness at temperatures below 0 °C.

    Representative property positioning of Indian Oil PP Homopolymer 1030FG against adjacent polypropylene grades. Values are typical commercial ranges, not certified specification limits.
    PropertyTest standard1030FGLow-MFR homo gradeRandom copolymer
    Melt mass-flow rateISO 1133-1:202210.0 g/10 min2.0–3.5 g/10 min4.0–10.0 g/10 min
    Tensile stress at yieldISO 527-2:201233–36 MPa32–36 MPa24–28 MPa
    Flexural modulusISO 178:20191,400–1,600 MPa1,250–1,550 MPa800–1,100 MPa
    Notched Izod impact at 23 °CISO 180:20232.0–3.5 kJ/m²3.0–5.0 kJ/m²5.0–10.0 kJ/m²
    Melting peakISO 11357-3:2018160–165 °C160–166 °C130–148 °C
    Heat deflection temperature at 0.45 MPaISO 75-2:201390–100 °C90–100 °C70–85 °C

    At the tooling level, the grade permits reduced wall thickness but requires adequate venting. Vent depths of 0.020–0.035 mm are standard for polypropylene homopolymer; deeper vents are avoided because the low melt strength can flash at the parting line when injection velocity exceeds 300 mm/s. Gate diameter is typically 40–60 % of the wall thickness for rectangular edge gates, and cold slug wells are sized to capture the lower-viscosity first melt front, which otherwise generates flow marks and jetting. Machine selection should follow a clamp-force requirement of approximately 3.0–5.0 kN/cm² of projected area for multicavity layouts, adjusted for cavity pressure at the targeted melt temperature.

    In thin-wall multicavity closures and disposable food-container production, the grade’s MFR of 10.0 g/10 min is used to shorten flow-path transit in tools with 0.5–1.0 mm wall sections. On a 180-tonne hydraulic injection moulding machine equipped with a 24:1 L/D general-purpose screw, barrel settings are commonly maintained at 180–200 °C in the feed zone, 200–220 °C in the compression zone, and 210–230 °C in the metering zone, with the nozzle at 220–240 °C. Holding pressure is typically set at 35–50 % of the peak injection pressure, and mould temperature is kept between 20 °C and 40 °C to balance crystallinity development against cycle time. A cushion of 3.5–5.0 mm is maintained because the high-flow front becomes sensitive to transfer-position drift; insufficient cushion produces gate blush and sink-mark variation, while excessive cushion increases residence time and can generate screw-recovery overrun.

    Screw-Recovery Overrun, Shrinkage Anisotropy and Rheological Boundaries

    On production-scale reciprocating-screw machines above 120 tonnes clamp force, the low viscosity of 1030FG at 230 °C permits high screw rotation speeds but increases risk of screw-recovery overrun if back pressure is set below 5 bar hydraulic. Field records from 32-cavity hot-runner cap moulds show that short nozzles with high heat input can drool during decompression; a decompression stroke of 2–4 mm and nozzle shut-off needles are common mitigations. Post-mould shrinkage in the flow direction is typically 1.2–1.8 % and cross-flow shrinkage 1.4–2.0 % after 48 h at 23 °C under ISO 294-4:2018; differential shrinkage in thick bosses and ribs drives warpage. To reduce anisotropic dimensional change, gate location is placed to maintain radial flow from a central sprue, and cooling circuits are balanced to a temperature delta of ±1.5 °C. Melt residence time above 260 °C should be limited because oxidative chain scission shifts MFR upward and produces yellowing, particularly at hot-runner drops with dead zones.

    For integral hinge geometries in closure tethers and flip-top caps, the grade is processed with a hot hinge section at 40–60 °C to orient the lamellae across the hinge. The homopolymer structure allows repeated flexural loading without stress whitening at the hinge root, but the notch sensitivity of the base polymer remains high at sub-zero temperatures. When impact-modified grades are not used, design should avoid sharp internal radii, weld-line traps at flow re-convergence, and heavy sections exceeding 6 mm, which extend cooling time by approximately 2.5–4.0 s/mm and increase sink-mark severity.

    When Food-Contact Compliance and Additive Interactions Constrain the Moulding Window

    Because the FG designation is used for food-contact articles, the formulation is aligned with olefin polymer requirements in FDA 21 CFR 177.1520 for polypropylene, and finished articles are typically evaluated under the overall migration and specific migration provisions of Regulation (EU) No 10/2011. The overall migration limit for plastic food-contact articles is 10 mg/dm²; compliance is tested with simulants selected for the intended food type and contact duration, and a declaration of compliance should be obtained from the producer for the specific batch. However, the homopolymer’s upper service temperature in hot-filled or microwave reheating applications must be kept below the article-specific heat distortion threshold because distortion under load can alter the contact surface and affect seal integrity. Pre-drying at 80 °C for 2–4 h is advised when ambient relative humidity exceeds 60 % or when hygroscopic masterbatches are added; free moisture at the feed throat causes intermittent screw slippage and creates melt-pressure oscillation. The base grade should not be combined with copper-based processing aids because copper ions accelerate autoxidative chain scission in polypropylene at processing temperatures above 200 °C; similarly, peroxide masterbatches used for controlled rheology adjustment require strict melt-temperature containment because uncontrolled visbreaking shifts MFR upward and erodes impact strength.

    Outdoor use of unmodified polypropylene homopolymer is constrained by photo-oxidative chain scission. Without ultraviolet stabilisation, prolonged UV-B exposure embrittles the surface within a single exposure season in aggressive climates. Articles that must withstand direct sunlight therefore require additional UV-stabiliser masterbatches or hindered amine light stabiliser packages, and the appropriate dosage must be validated by accelerated weathering under ISO 4892-2:2013 or equivalent. For coloured food-contact articles, pigment masterbatches should be selected only after confirmation that the carrier resin and pigment additives do not raise overall migration above the relevant limit for the intended simulant. The grade is not inherently flame retardant and is not a substitute for grades rated under UL 94 when a specific flammability classification is required.

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