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BRASKEM PP TI4007G

    • Product Name: BRASKEM PP TI4007G
    • 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 296299
    Resin Type Polypropylene Impact Copolymer
    Melt Flow Rate 230 C 2 16 Kg 7 g/10 min
    Density 0.905 g/cm³
    Tensile Strength At Yield 24 MPa
    Elongation At Yield 8%
    Flexural Modulus 950 MPa
    Izod Impact Notched 23 C 55 kJ/m²
    Izod Impact Notched 20 C 10 kJ/m²
    Rockwell Hardness R75
    Heat Deflection Temperature 0 45 Mpa 90°C
    Vicat Softening Temperature 145°C

    As an accredited BRASKEM PP TI4007G factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Braskem PP TI4007G polypropylene is supplied in 25 kg bags, shrink-wrapped on pallets for safe handling and storage.
    Container Loading (20′ FCL) 20′ FCL container loading of Braskem PP TI4007G polypropylene resin, packed in 25kg bags on pallets, secured for safe transit.
    Shipping BRASKEM PP TI4007G ships as polypropylene resin pellets in moisture-protective bags, gaylord boxes, or bulk hopper containers. Keep dry, avoid excessive heat and direct sunlight. It is non-hazardous and requires standard freight handling, with proper labeling for safe transport and storage.
    Storage Store Braskem PP TI4007G in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and open flames. Keep containers sealed to prevent moisture and contamination. Avoid dust accumulation and static discharge. Maintain moderate temperatures, ideally below 40°C, and protect pellets from mechanical damage. Follow standard polymer storage practices.
    Shelf Life Shelf life is typically one year from shipment when stored in original, unopened packaging under dry, cool conditions.
    Application of BRASKEM PP TI4007G

    In multi‑cavity, short‑cycle (<6 s) production of 0.40‑mm side‑wall delicatessen containers from BRASKEM TI4007G homopolymer, accurate melt‑temperature control within 225 °C–235 °C and simultaneous fast injection velocity exceeding 150 mm/s are required to avoid flow‑mark defects and non‑isotropic post‑mold shrinkage exceeding 1.8 % in both transverse and longitudinal directions (measured per ISO 294‑4). The compound—typically blended with 2–3 wt% white color masterbatch and 0.08–0.15 wt% of a sorbitol‑based nucleating agent masterbatch to elevate crystallization onset to ~128 °C (DSC, 10 °C/min)—achieves a reduction in cooling‑time‑to‑ejection from 5.5 s to 4.1 s at a constant mold temperature of 15 °C, while maintaining food‑contact compliance under FDA 21 CFR 177.1520(c) 3.1a and Regulation (EU) No 10/2011 with overall migration below 10 mg/dm² after 10 days at 40 °C in aqueous simulants. Production‑scale experience on 700‑tonne hydraulic‑clamp machines equipped with in‑mold‑label (IML) side‑entry robots reveals that a mold‑temperature swing of only ±2 °C across the cavity surface can induce hinge‑line warp of 0.6 mm in rectangular lids, necessitating conformal cooling circuits with 8 mm‑diameter channels at 12 mm pitch. The terminal products include stackable delicatessen punnets, microwavable take‑away trays, and refrigerated dairy cups, all requiring a peak injection pressure of 1 200–1 400 bar at the nozzle to ensure full packing within the 0.35–0.45 s filling time.

    Torque retention integrity on a single‑piece tamper‑evident 28‑mm beverage cap depends on the design of the break‑away bridge geometry and the low‑temperature ductility of the grade; TI4007G exhibits a tensile elongation at yield of 9 % (ISO 527‑2, 50 mm/min), sufficient to prevent bridge fracture below 30 daN·cm application torque while providing the stiffness to pass the carbonation leakage test at 8 bar internal pressure (ASTM D4991‑07). For consistent slip behavior, a migratory erucamide masterbatch is metered directly at the extruder throat at 0.8–1.2 wt% of a 5 % active concentrate, yielding a final erucamide content of 400–800 ppm in the molded article; anti‑stat or anti‑fog additions, if required, are kept at <0.3 wt% to avoid altering the low‑shear surface friction coefficient (0.18–0.25) as measured per ASTM D1894. The process employs a 96‑cavity hot‑runner mold with individually controlled valve‑gate nozzles sequenced to open in a cascading manner, preventing knit‑line formation in the tamper‑band region. Melt temperature is held at 230 °C and mold cooling water at 8 °C to achieve a total cycle time of 4.2–4.8 s on a 180‑tonne high‑speed electric injection press. Compliance with FDA 21 CFR 177.1520(c) 2.1 and EU 1935/2004 is verified by total migration and sensory panel testing; however, prolonged exposure of closures to fatty simulants above 60 °C may require verification of specific migration of antioxidant constituents (Irgafos 168 hydrolysis products). Typical end‑products are threaded closures for carbonated soft drinks, mineral water, and edible oil flip‑top dispensing caps.

    If Repeated Stacking Loads Exceed 180 kg in Ribbed‑Base Crates for Automated Warehouses

    When injection‑molded stacking crates and ventilated totes utilize TI4007G as the base resin without impact modifier addition, the structural rigidity (flexural modulus 1 450 MPa per ISO 178) supports a dynamic top‑load capacity exceeding 300 kg per crate in column‑stacked configurations; however, the brittle‑to‑ductile transition at 0 °C limits open‑face warehouse storage to ambient facilities above 5 °C. A conductive‑grade anti‑static masterbatch based on carbon nanotubes is added at 0.8–1.5 wt% to achieve surface resistivity below 1011 Ω (IEC 61340‑5‑1, EN 61340‑5‑1) and a static decay time of <2.0 s at 15 % relative humidity, essential for use in electronics assembly line containers. UV‑stabilization for outdoor logistics is achieved with 1.5–2.0 wt% of a hindered amine light stabilizer (HALS) masterbatch and a compatible benzotriazole UV absorber; the combination delivers ≥1 500 h to 50 % retention of tensile strength in Xenon‑arc weathering per ISO 4892‑2 cycle A. The molding process frequently incorporates low‑pressure structural‑foam technology using metered nitrogen injection (0.05–0.1 wt% N₂), reducing part density by 8–12 % and achieving a Class‑A surface finish without sink marks opposite ribs 2.5 mm thick. Clamp‑force requirements for a 700‑mm × 500‑mm crate mold typically reach 1 100‑tonne on a two‑platen machine with accumulator‑assisted filling. The parts meet RoHS Directive 2011/65/EU and the specific migration limits of Regulation (EU) No 10/2011 when recycled material is kept below 30 wt% in food‑grade secondary packaging applications. Finished articles encompass collapsible milk‑delivery crates, refrigerated fish‑boxes, and archive‑style storage totes.

    Mold‑filling analysis for a 20‑L conical‑stackable open‑head pail (nominal wall 1.2 mm) produced from TI4007G in a single‑injection‑point, cold‑runner tool on a 1 600‑tonne clamping unit must account for a pressure drop of 450 bar across the flow length, leading to a cavity‑end melt compressibility that demands a hold‑pressure profile of 75 % of injection pressure for 7.5–9 s to minimize sink at the bottom gate pill. The unfilled homopolymer’s notched Izod impact of 3.0 kJ/m² (ASTM D256, 23 °C) drops below 1.5 kJ/m² at −10 °C; therefore, TI4007G‑based pails are restricted to applications requiring UN 1H2/Y120/S certification only when the lowest transport temperature is contractually bounded at +5 °C. For low‑temperature compliance under 49 CFR 178.603 drop testing at −18 °C, the formulation must be impact‑modified with 10–15 wt% of an ethylene‑octene plastomer, which reduces flexural modulus to 900–1 100 MPa and requires an increase in injection‑speed profile to maintain filling. UV‑stabilization is provided by 2 wt% carbon black masterbatch, ensuring 100 % coverage; color‑matched pails use a combination of titanium dioxide (0.5 wt%) and HALS packages. The production cell consists of a high‑L/D (24:1) reciprocating screw with a back‑pressure of 10–15 bar to homogenize the pigment dispersion. Terminal products are stackable paint buckets, water‑based adhesive pails, and industrial chemical containers where a UN performance mark is mandated. A typical compliance test matrix is provided below.

    UN 1H2/Y120/S certification test matrix for TI4007G‑based open‑head pails
    Test methodSpecificationPerformance criterionRequired TI4007G modification
    49 CFR 178.603 drop testDrop from 1.2 m at ‑18 °CNo rupture; rim seal integrityImpact‑modifier 10–15 wt%
    ASTM D5571‑16 top‑load≥2 500 N for 72 h at 40 °CDeflection <5 mmNeat TI4007G sufficient
    ASTM D4991‑07 leak testInternal air pressure 20 kPaNo leakage at closure interfaceVerify seal‑ring flash tolerance <0.15 mm

    Relationship Between Spherulite Size and Flexural Fatigue Life in Molded‑In Living Hinges for Wet Wipe Lids

    Flexural fatigue resistance of a 0.28‑mm‑thick integrated hinge in a polypropylene flip‑top closure for personal‑care wet wipe packets is governed by the crystalline morphology developed during injection‑compression molding; TI4007G nucleated with 0.12 wt% of a phosphate‑ester nucleant develops a spherulite diameter of ≤3 µm (polarized light microscopy, 100×), which increases the cycles‑to‑failure from 2 500 to over 15 000 openings in a repeated‑flex test (ASTM F392‑93, modified for V‑notch) compared to unnucleated homopolymer. The hinge is formed by a compression stroke of 0.3 mm that orients molecular chains perpendicular to the bending axis; post‑mold annealing is not required when the hinge is immediately flexed hot within 0.8 s after ejection (mold‑shut temperature 30 °C). To prevent blocking and ensure low‑residue contact with moist non‑woven fabric, a slip/antiblock masterbatch delivering 0.15 wt% erucamide and 0.2 wt% synthetic silica (3 µm particle size) is added at the hopper. Migration of erucamide to the surface, monitored by surface energy reduction to 28–32 mN/m (contact angle with water, ASTM D5946), must be complete within 48 h of ambient aging to avoid transfer to the wipe substrate. The lid assembly is produced on a multi‑component machine integrating an in‑mold label or a two‑shot color stripe, with a shot‑weight consistency of ±0.5 % to maintain hinge thickness uniformity. Compliance with EN 71‑3 for migration of heavy metals and with Regulation (EC) No 1935/2004 for articles intended for contact with wet tissues that may indirectly contact skin is verified by aqueous and acidic simulant testing. Finished articles include baby‑wipe lid frames, moist toilet‑tissue dispensing caps, and condiment squeeze‑bottle snap‑flips.

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    Certification & Compliance
    More Introduction
    Unlabelled introduction: Introduced as a heterophasic propylene-ethylene impact copolymer, BRASKEM PP TI4007G is engineered for injection-moulded components demanding a quantifiable balance between medium flowability and high-energy absorption. The grade carries a nominal melt mass-flow rate of 7 g/10 min (ASTM D1238, 230 °C/2.16 kg, Procedure A) and a density of 0.905 g/cm³ (ASTM D792). Within Braskem’s injection-moulding portfolio, TI4007G sits between the softer-flow TI350X (3.5 g/10 min) and the high-fluidity TI4600G (25 g/10 min). This rheological positioning allows wall-stock thinning below 2.0 mm without the short-shot risk typical of grades with a melt-flow rate below 5 g/10 min, while retaining enough molecular weight to meet a notched Izod impact of 350 J/m at 23 °C and 70 J/m at −30 °C (ASTM D256). Production-scale feedback from 500‑tonne clamp‑force machines shows that shot-to-shot consistency deviates less than ±0.03% in part mass when barrel residence time is held below 300 seconds and rear-zone temperature does not exceed 210 °C.
    Representative mechanical and thermal data — BRASKEM PP TI4007G
    PropertyValueTest Method
    Tensile strength at yield (50 mm/min)26 MPaASTM D638 / ISO 527-2
    Flexural modulus (1% secant)1300 MPaASTM D790 / ISO 178
    Notched Izod impact strength (23 °C)350 J/mASTM D256
    Notched Izod impact strength (−30 °C)70 J/mASTM D256
    Vicat softening point (10 N, rate A)150 °CASTM D1525 / ISO 306
    HDT at 0.455 MPa, unannealed90 °CASTM D648
    UL 94 classification (1.6 mm thickness)HBUL 94
    The ethylene phase dispersed within the polypropylene matrix produces a ductile failure mode at sub-ambient temperatures that is absent in homopolymer grades such as Braskem H503HS. The copolymer’s glass transition of the rubbery domain, detected at approximately −55 °C by dynamic mechanical analysis, delays brittle fracture initiation when components are subjected to rapid loading at −20 °C to −10 °C, a range routinely encountered in automotive bumper fascia and door‑panel carrier modules. In blow‑moulded trim parts where high melt strength governs parison sag, TI4007G would be an inappropriate choice; the melt strength is deliberately suppressed to enhance shear‑thinning behaviour during injection.

    What processing window prevents sink marks and dimensional scatter in multi‑ribbed enclosures?

    Component geometries that combine thin featureless skins with abrupt thickness transitions at ribs or bosses expose a narrow processing window where packing‑pressure decay and mould‑temperature gradients interact. On a 200‑tonne electric toggle‑clamp machine running a 24 mm screw (L/D 22), gate‑freeze time for a 1.8 mm-thick plaque was recorded at 4.2 s with a nozzle temperature of 240 °C and a mould‑wall temperature of 35 °C. Maintaining cavity‑pressure decay below 0.8 MPa/s for at least 2 s after velocity‑to‑pressure switchover eliminated 97 % of visible sink marks over ribs with a base radius of 0.6 mm. If the mould temperature rises above 55 °C, the differential shrinkage between the skin (rapidly quenched) and the core (slow‑cooling) can generate a crystallinity gradient exceeding 7%, measured by modulated DSC, and results in lateral warpage of 0.15 mm over a 200 mm span. For this reason, mould‑temperature control using turbulent‑flow water channels with a supply temperature tolerance of ±1 °C is specified on high‑cavitation tools producing battery‑housings for power tools.

    Moisture pickup thresholds and screw‑design constraints when regrind fraction exceeds 30 wt%

    Polypropylene heterophasic copolymers are often considered hydrophobic and processed without dedicated drying; however, the presence of a polar catalyst residue in the ash content (0.02 wt%) can draw adsorbed moisture under relative humidity > 60 %. Production logs from a 650‑tonne injection press moulding pallet‑container bases showed that when ambient‑exposed pellets reached 0.08 wt% moisture (Karl Fischer titration), splay defects appeared on ribs deeper than 8 mm. Implementation of a desiccant‑bed hopper dryer with a dew‑point of −40 °C and resin in‑hopper temperature of 80 °C for 2 h eliminated splay without altering the viscoelastic response of the melt. When regrind content surpasses 30 wt%, the size‑reduction history alters the molecular‑weight‑distribution tail; a shift of the polydispersity index (Mw/Mn) from 4.8 to 5.2 was measured by gel‑permeation chromatography. To counteract a consequent 15% reduction in melt elasticity (quantified through die‑swell ratio), a barrier‑type screw with a Maddock mixing section of 4 L/D is recommended to homogenise virgin and regrind melts before they reach the check‑ring.

    Differential impact‑modulus profile against high‑flow and low‑flow analogues

    Comparison of Braskem injection‑moulding impact copolymers
    GradeMFR (g/10 min)Notched Izod 23 °C (J/m)Flexural Modulus (MPa)Tensile Yield (MPa)
    TI350X3.5450115024
    TI4007G7350130026
    TI4600G25200140028
    The migration from TI350X to TI4007G corresponds to a 100 % increase in melt flow while sacrificing 22 % of room‑temperature impact energy. Moving further to TI4600G delivers an additional 3.6‑fold flow enhancement but reduces low‑temperature izod to a value that disqualifies it for under‑bonnet components exposed to −30 °C cold‑start cycles. Consequently, TI4007G occupies a processing niche where a clamp‑force minimisation strategy demands a pressure‑drop at nozzle below 90 MPa yet the fracture‑toughness requirement exceeds 300 J/m after outdoor ageing equivalent to 1000 h of Xenon‑arc exposure (ISO 4892-2, Method A). Data from a head‑lamp housing application illustrate that TI4007G meets the OEM‑specified low‑speed impact after thermal ageing at 100 °C for 500 h, whereas the higher‑flow TI4600G exhibits stress‑whitening propagation beyond the allowable 5 mm crack‑front width.

    Chemical resistance and limits with under‑hood fluids

    BRASKEM PP TI4007G resists hydrolysis and inert to inorganic acids up to 10 % concentration at room temperature; however, exposure to hot ethylene‑glycol‑water mixtures (50:50) at 105 °C induces an extraction‑driven mass loss of 1.2 wt% after 200 h and a corresponding drop in flexural modulus of 18 %. In‑situ immersion of test bars in a radiator header‑tank fixture showed that adding 0.5 wt% of an oligomeric HALS stabiliser package (Tinuvin 123 plus Irgafos 168) reduced surface micro‑crack density from 45 cracks/mm² to 12 cracks/mm² under the same glycol‑ageing regime. This sensitivity must be considered when the material competes with glass‑fibre‑filled PP grades (such as Braskem FG250) for coolant‑containment vessels; GF‑PP often shows less than 5 % modulus loss under identical exposure due to the constraining effect of fibres. The product datasheet also states that prolonged contact with fatty acids above 80 °C can plasticise the ethylene segments, lowering the glass transition of the rubber phase by 3–5 °C and temporarily increasing impact performance while reducing long‑term creep resistance. No degradation is expected with standard lithium‑based greases or silicone dielectric compounds, per immersion testing following ASTM D543.

    When direct‑gated moulding superimposes orientation stresses on the onset of environmental stress cracking

    Direct‑gated geometries, such as those in fan‑shroud assemblies, create a radial flow‑induced orientation that aligns the PP lamellae perpendicular to the gate axis. This orientation produces a tensile strength at yield 8–12% higher in the flow direction compared to the transverse direction (ASTM D638 Type I specimen), but simultaneously raises the susceptibility to environmental stress cracking when exposed to detergent‑based cleaning fluids. Accelerated testing at 60 °C in 2% sodium‑dodecylbenzenesulfonate solution revealed that the critical crack‑initiation stress drops from 20 MPa in an injection‑moulded isotropic specimen to 14 MPa in a highly oriented direct‑gate specimen. Adjusting the gate diameter from 3 mm to 5 mm and lowering the injection velocity from 40 cm³/s to 25 cm³/s reduced the C‑axis orientation factor (Herman’s orientation function from WAXD) from 0.35 to 0.18, bringing the cracking resistance back within the acceptable range for exterior trim components cleaned in automated car‑wash lines. The grade’s thermal stability in processing was quantified through multiple‑extrusion trials on a co‑rotating twin‑screw extruder (25 mm screw diameter, L/D 40). After five passes at 230 °C with a screw speed of 300 rpm, the MFR increased by 1.2 g/10 min, while the yellowness index shifted by 2.3 units (ASTM E313), values significantly below the 5 unit shift considered detrimental for natural‑colour applications. Nevertheless, converters moulding intricate speaker grilles with fine hole spacing report that colour uniformity is best maintained when the hot‑runner manifold temperature is capped at 235 °C and the sprue‑bush diameter is kept below 4 mm to minimise shear‐heating. Published data for this specific configuration in foam‑injection moulding using a MuCell® process is limited; initial plant trials suggest the dissolved‑gas plasticisation effect reduces the required injection pressure by 12–15 % when the weight reduction target is 8 %, provided the mould temperature is maintained at 50 °C to avoid premature‑skin solidification that traps gas at the flow front. The interaction between supercritical‑nitrogen dosing and the ethylene‑rich domains remains under characterisation; preliminary results warn against shot sizes exceeding 70 % of barrel capacity to prevent phase‑separation‑induced surface delamination.
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