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TASNEE PP H1045

    • Product Name: TASNEE PP H1045
    • 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 936864
    Material Type Polypropylene Homopolymer
    Melt Flow Rate 230 C 2 16 Kg 45 g/10 min
    Density 0.905 g/cm³
    Tensile Strength At Yield 33 MPa
    Elongation At Yield 10 %
    Flexural Modulus 1500 MPa
    Izod Impact Strength Notched 23 C 3.5 kJ/m²
    Heat Deflection Temperature 1 8 Mpa 65 °C
    Heat Deflection Temperature 0 45 Mpa 100 °C
    Vicat Softening Temperature 10 N 152 °C
    Rockwell Hardness R95

    As an accredited TASNEE PP H1045 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing TASNEE PP H1045 polypropylene is supplied in 25 kg multi-wall paper bags, palletized and shrink-wrapped for safe handling.
    Container Loading (20′ FCL) 20′ FCL shipment of TASNEE PP H1045 polypropylene pellets, loaded in jumbo bags on pallets and secured for safe transport.
    Shipping TASNEE PP H1045 is a polypropylene resin shipped as non-hazardous, free-flowing pellets. It is typically packed in 25 kg bags, big bags, or transported via bulk hopper containers. Protect from moisture, direct heat, and contamination; store in a dry, ventilated area to preserve product quality.
    Storage Store TASNEE PP H1045 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture contamination and dust accumulation. Segregate from strong oxidizing agents. Maintain good housekeeping to avoid spillage, and follow standard industrial hygiene practices when handling.
    Shelf Life TASNEE PP H1045 has a shelf life of 12 months from delivery when stored properly in original, unopened packaging under dry, cool conditions.
    Application of TASNEE PP H1045

    In thin-wall food packaging tooling, the selection of TASNEE PP H1045—a high-flow polypropylene homopolymer with nominal MFR of 45 g/10 min at 230 °C/2.16 kg under ISO 1133-1:2022—is driven by the need to fill wall-thickness distributions of 0.4–0.8 mm without exceeding injection pressure ceilings in hot-runner multi-cavity tools. Compliance boundaries for direct food contact are set by FDA 21 CFR 177.1520(c), EU Regulation (EC) No 10/2011 with an overall migration limit of 10 mg/dm² for the finished article, and GB 9685-2016 additive positive-list requirements for shipments routed to China; REACH SVHC screening is applied at 0.1% w/w under Article 33 obligations. Typical formulation starts from 100 phr H1045 base resin, with a nucleating agent masterbatch dosed at 0.05–0.20 phr to shift crystallization onset and reduce demolding time, an acid scavenger at 0.02–0.10 phr to protect residual catalyst residues, and a food-contact color masterbatch at 1.0–3.0 phr. Downstream production runs on injection molding machines with screw L/D ratios of 20:1–25:1 and compression ratios between 2.0:1 and 2.5:1, using melt temperatures of 230–260 °C, mold temperatures of 15–40 °C, injection speeds of 300–500 mm/s, and packing pressures of 30–50 MPa; cycle times fall between 4 s and 8 s for 0.5 mm nominal walls. Production-scale behavior shows that gate-to-gate fill imbalance above 2% in 48-cavity valve-gated tools produces visible flow hesitations and short-shot tendencies, while mold temperature above 40 °C extends cooling time without proportionate improvement in part flatness. Terminal articles include deli cups, dairy containers, snack tubs, and matching lids; H1045 should not be selected for hot-fill or retort conditions above 90 °C, nor for high-fat applications requiring long-chain triglyceride oxygen barriers beyond polypropylene homopolymer permeability.

    How Does H1045 Grade Selection Impact High-Cavitation Closure Molding?

    On 72-cavity valve-gated closure molds, H1045 is evaluated primarily for its ability to fill thin tamper-band bridges and thread profiles under short pack-and-hold windows, although published peer-reviewed pressure-drop data specific to this grade in high-cavitation closure tooling is limited to converter internal qualification records rather than public literature. Compliance documentation for food and beverage closures references FDA 21 CFR 177.1520, EU Regulation (EC) No 10/2011, EN 1186-1:2002 overall migration test protocols, and ASTM D2063/D2063M-10(2017) torque retention measurement; closures for household chemical or detergent applications require additional assessment under ISO 8317:2015 child-resistant package torque and opening-force verification. Formulation addition ratios in high-cavitation caps are built on 100 phr H1045, with erucamide slip masterbatch at 0.05–0.15 phr to control denesting and application torque, primary phenolic/phosphite antioxidant at 0.04–0.12 phr, nucleating or clarifying masterbatch at 0.10–0.25 phr, and antistatic concentrate at 0.10–0.40 phr where dust pick-up on transparent closures is a customer rejection criterion. Processing uses electric or hybrid machines with clamp forces from 150 t to 350 t, screw diameters selected for 80–120 rpm surface speeds, melt temperatures of 220–250 °C, back pressures of 5–10 bar, and cycle times of 4.5–8.0 s; hot runner drops are balanced to ±1 °C or less to avoid differential gate freeze-off that distorts tamper-band elongation. Failure modes observed in production include thread flattening when demolding temperature exceeds 75 °C and loss of seal-cap spring-back when packing time is shortened below 0.3 s in 0.5 mm tamper bridges. Terminal products are still-water and juice beverage closures, snap-on dairy caps, and non-beverage household chemical caps where torque and dimensionally stable threads are required.

    When Dimensional Stability in Thin-Wall Labware Overrides Aesthetic Transparency

    In polypropylene homopolymer labware such as pipette tips, reagent reservoirs, and microcentrifuge tube bodies, optical clarity is subordinate to demolding repeatability and liquid handling tolerances, and the high-flow MFR class of H1045 reduces orientation stress in 0.2–0.5 mm tip orifice walls. Compliance anchors for laboratory consumables intended for diagnostic or research workflows include ISO 10993-5:2009 cytotoxicity testing when the article is declared as a medical accessory, USP Class VI testing for plastic containers and closures, ISO 13485:2016 quality management system requirements for manufacturers placing devices into regulated markets, and REACH SVHC certification; where export to China is required, GB/T 16886.5-2017 may be invoked for cytotoxicity equivalence. The formulation window uses 100 phr H1045, a clarifier masterbatch at 0.10–0.30 phr where semi-translucent walls are acceptable, an antioxidant system at 0.05–0.15 phr to survive gamma irradiation at 25–50 kGy without excessive yellowing, and a high-purity erucamide-free lubricant at 0.05–0.20 phr because erucamide migration can interfere with low-binding PCR and diagnostic reactions. Molding of pipette tips requires high-speed hydraulic or electric injection units with screw L/D near 20:1, melt temperatures of 220–250 °C, mold temperatures of 15–25 °C, injection pressures of 80–120 MPa, and hold times sufficient to prevent sink at the tip gate; tooling must be polished to SPI A1 or diamond-bright levels and run in ISO 14644-1 cleanrooms of Class 7 or 8 when assembled tips are packaged without post-molding washing. Production bottlenecks include core shift exceeding 0.03 mm on long, thin core pins when melt temperature is too low, and gate blush at the tip orifice when injection velocity exceeds 500 mm/s. Terminal finished products include graduated pipette tips, reagent reservoirs, microcentrifuge tubes with snap caps, and assay plate adapters made from unfilled H1045 homopolymer.

    Rigid houseware programs running H1045 typically route through multi-cavity open-nozzle tools where wall thickness stays above 1.2 mm and the limiting criterion is dimensional stability after demolding rather than fill pressure. Compliance obligations for drawer organizers, stackable storage totes, and refrigerator containers sold into European and North American markets include FDA 21 CFR 177.1520 for food-adjacent use, LFGB §30 and §31 for German food-contact enforcement, and EN 71-3:2019+A1:2021 migration limits for certain toy-like children’s storage items; the grade must be evaluated for phthalate-free, heavy-metal, and PAH restrictions under REACH Annex XVII entries covering plasticized materials and articles. Formulation starts at 100 phr H1045 homopolymer, but where low-temperature drop impact at 0 °C is specified, converters let down an external polyolefin elastomer at 5–12 phr, accepting reductions in flexural modulus of 8–15% as measured by ISO 178:2019; for stackable totes, a nucleating agent at 0.05–0.15 phr and an antistatic masterbatch at 0.5–1.5 phr are used to control cycle-to-cycle wall thickness variability and dust attraction during warehouse storage. Injection molding uses melt temperatures of 210–240 °C, mold temperatures of 20–40 °C, injection pressures of 60–100 MPa, and pack/hold switching based on screw position rather than time to avoid sink over strengthening ribs; cooling time for 1.5 mm nominal walls ranges from 8 s to 15 s. Field data show that rib-to-wall ratios above 0.7:1 produce visible sink and warpage unless mold temperature is lowered to 15 °C, which then raises post-shrinkage angular deviation by 0.3–0.5 ° in large flat side panels. Terminal products are refrigerator drawer organizers, wardrobe storage boxes, stackable utility totes, and desk accessory trays made from unfilled H1045 with post-industrial regrind ratios generally below 20 wt%.

    Small Appliance Structural Brackets and Glow-Wire End-Use Compliance

    For non-load-bearing internal appliance brackets, cable management channels, and drainage conduits, H1045 is selected for thin-wall rigidity and resistance to continuous service temperatures up to 90 °C under IEC 60216-1:2013 thermal endurance principles, though final part approval depends on glow-wire and flame class testing. Compliance standards for electrical-adjacent polypropylene components include IEC 60695-2-11:2021 glow-wire flammability test for end products, UL 94 HB at 3.0 mm nominal thickness as a baseline, IEC 62321 RoHS substance screening for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE, and REACH SVHC declaration; when the part is used in direct contact with food contact surfaces, FDA 21 CFR 177.1520 still applies but electrical standards take precedence for molded-in wire clips. Formulation uses 100 phr H1045 for natural and colored unfilled brackets; flame retardant masterbatch based on halogen-free ammonium polyphosphate or intumescent chemistry is added at 6–20 phr where UL 94 V-2 or V-0 is required, with measurable loss in tensile yield strength of 10–25% as tested by ISO 527-2:2012. Process settings on 80–250 t injection molding machines include melt temperatures of 220–245 °C, mold temperatures of 20–35 °C, back pressures of 4–8 bar, and injection velocities profiled to 120–250 mm/s to avoid shear-induced degradation of the flame retardant package; respiration of the mold must be controlled because intumescent systems generate moisture and plate-out on tool surfaces after 6–8 h continuous running, requiring periodic wiping. Dimensional acceptance criteria for screw bosses and snap-fit lugs are typically ±0.05 mm for holes, with post-mold shrinkage of 1.2–1.6% in flow direction and 0.8–1.2% cross-flow after 48 h at 23 °C per ISO 294-4:2018. Terminal products are vacuum cleaner internal brackets, tabletop appliance drainage manifolds, cable management clips, and washing machine lint-filter housings where unfilled polypropylene homopolymer is acceptable.

    Because disposable cutlery tooling demands high shear through side gates and thin flash-prone profiles, the high-flow MFR class of H1045 enables filling of fork tines and spoon bowl edges at wall thicknesses as low as 0.7 mm without brittle weld lines, but the material is limited to unheated food contact and cannot withstand oven or microwave use above 100 °C. Food-contact compliance for disposable cutlery sold to EU and US markets is governed by FDA 21 CFR 177.1520, EU Regulation (EC) No 10/2011 including overall migration limits of 10 mg/dm², EN 1186-1:2002 migration test protocols, and GB 9685-2016 for China-bound stock; converters exporting to Japan must verify compliance with Japan Food Sanitation Law utensils, containers, and packaging standards. Formulation ratios use 100 phr H1045, a nucleating agent at 0.05–0.20 phr to maintain rapid crystallization, a slip masterbatch at 0.10–0.30 phr for denesting, and a white masterbatch at 1.5–3.0 phr; black cutlery may incorporate carbon black masterbatch at 0.8–2.0 phr but only food-contact-approved carbon black grades are permitted. Processing on high-speed injection molding machines with clamp force from 100 t to 250 t uses melt temperatures of 230–260 °C, mold temperatures of 15–30 °C, injection speeds of 250–450 mm/s, and cycle times of 6–10 s in 32-cavity to 64-cavity stack or side-entry molds; flash formation at the fork tine tips is controlled by holding velocity at 80–90% of maximum during final fill and by maintaining cavity steel flatness within 0.02 mm. Terminal finished products are disposable forks, spoons, knives, and combined spork utensils for airline meal service, takeaway foodservice, and institutional catering where cold or warm food contact does not exceed 80 °C for more than 2 h.

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    Certification & Compliance
    More Introduction

    TASNEE PP H1045 is a propylene homopolymer injection-moulding grade with a nominal melt flow rate of 45 g/10 min under ISO 1133-1:2022 at 230 °C and 2.16 kg. The homopolymer backbone contains no ethylene comonomer, which distinguishes its phase morphology from heterophasic copolymers. Typical published density under ISO 1183-1 is 0.905 g/cm³. Tensile stress at yield under ISO 527-2 is approximately 36 MPa, flexural modulus under ISO 178 is approximately 1800 MPa, and notched Izod impact strength under ISO 180/A at 23 °C is approximately 2.0–2.5 kJ/m². Vicat softening temperature under ISO 306/A50 is approximately 154 °C, while heat deflection temperature under ISO 75-2/B at 0.45 MPa is approximately 95 °C. Tensile strain at yield is approximately 8 %, and Rockwell hardness under ISO 2039-2 is approximately 100 R. Equivalent ASTM designations include ASTM D1238, ASTM D638, ASTM D790, and ASTM D648.

    The product is specified for thin-wall rigid packaging, caps, closures, housewares and small technical components in which filling lengths are long relative to wall thickness. For injection moulding, the standard processing window is 220–260 °C melt temperature and 10–40 °C mould temperature. The material does not require forced drying unless surface moisture exceeds 0.05 %, in which case a desiccant dryer at 80 °C for 2 h is used. The grade is supplied as pellets and should not be stored for prolonged periods above 40 °C under direct UV exposure. Because of the high melt flow rate, the grade is not intended for extrusion or blow moulding; parison melt strength is lower than that of a fractional-melt-index homopolymer.

    Does the 45 g/10 min Melt Flow Rate Shift the Injection Pressure–Cycle Time Relationship?

    The pressure–cycle time relationship in thin-wall PP moulding is governed by viscous pressure drop across the sprue, runner and cavity. At the same melt temperature, a melt flow rate of 45 g/10 min generates lower apparent viscosity than a 25 g/10 min homopolymer, which permits filling of 0.45 mm wall sections at hydraulic injection pressure reductions commonly observed in the range of 10–20 %. On a multi-cavity hot-runner system, the pressure reduction is not uniformly distributed. Cavities fed from the centre manifold may fill earlier than those at the periphery unless the manifold balance is adjusted for the lower viscosity. Screw recovery time is also shortened because lower shear viscosity reduces torque demand, but back pressure should be limited to 5–15 bar to avoid excessive shear heating and uncontrolled viscosity reduction.

    On a reciprocating-screw injection moulding machine with a 20:1 to 24:1 L/D barrier screw and compression ratio of 2.5:1, screw speed should be maintained in the range of 100–200 rpm. The high melt fluidity shortens gate freeze time; therefore, holding-pressure transfer, packing time and decompression settings require cavity-pressure verification. With valve-gated hot runners, premature gate opening produces flow lines around the gate. Valve pin movement should be verified with cavity-pressure sensors. For open hot tips, the gate diameter should not exceed 1.0 mm in thin-wall caps because delayed freeze creates gate stringing.

    Process conflicts occur at the upper melt temperature limit. Barrel set-points above 260 °C accelerate thermo-oxidative chain scission. At 270 °C, the melt flow rate can drift upward by more than 10 % within 5 min residence time, causing flash and loss of tensile properties. The front zone should therefore not exceed 250 °C during normal cycling. If a machine interruption exceeds 3 min, the barrel should be purged before restarting thin-wall production.

    Tensile Modulus and the Thin-Wall Stiffness Boundary in High-Flow Homopolymer PP

    In thin-wall rigid packaging, part stiffness is determined by flexural modulus and section geometry rather than by melt flow rate alone. The flexural modulus of 1800 MPa under ISO 178 provides adequate top-load performance in lids and tubs, but the absence of an elastomeric phase reduces notched Izod impact strength to approximately 2.0–2.5 kJ/m² at 23 °C. For cold-chain packaging or freezer applications, low-temperature impact must be evaluated separately; notched Izod at -20 °C is typically below 2.0 kJ/m². The product should not be used in applications requiring ductile fracture at sub-zero temperatures. An impact copolymer or lower-flow homopolymer with a rubber phase is required when the specification exceeds 3.0 kJ/m².

    The stiffness–toughness shift is not linear in melt flow rate. Reducing melt flow rate from 45 to 25 g/10 min raises notched Izod impact by only 0.5–1.0 kJ/m², while switching to a heterophasic impact copolymer can raise impact by more than 5 kJ/m². The grade is therefore suited to packaging where stiffness, heat resistance and fast filling dominate, but not to load-bearing parts subject to impact at low temperature. Recycled PP additions above 20 wt% can reduce effective melt flow rate and increase ash content. In thin-wall pilot trials, blends with post-industrial PP scrap having melt flow rate below 15 g/10 min reintroduced short-shot defects and required a barrel temperature increase of 10–15 °C to restore fill. Published data for this specific configuration is limited; converter trials should establish the maximum regrind level for a given tool.

    When High-Flow Homopolymer Replaces Random Copolymer in Opaque Rigid Packaging

    Random copolymer polypropylene is specified for transparency and a lower seal-initiation temperature. Replacement of a random copolymer with PP H1045 is technically feasible when opacity is acceptable and when the sealing step can tolerate a higher seal-bar temperature. The homopolymer has a higher Vicat softening point than many random copolymers, which improves hot-fill resistance but narrows the low-temperature sealing window. Seal-strength testing under ASTM F88/F88M is required to adjust dwell time and pressure. On high-speed packaging lines, seal bar temperatures must often be increased by 5–15 °C relative to random copolymer; incomplete fusion occurs at peel interfaces if sealing parameters are not adjusted.

    Optical clarity is not comparable. Homopolymer PP without an optical clarifying additive produces higher haze under ISO 14782 than clarified random copolymer grades. The difference in comonomer content also changes solvent resistance and organoleptic properties. The grade should not be substituted in clear beverage cups or transparent hinged lids without sealing and sensory validation.

    Compared with impact copolymers, PP H1045 has higher stiffness but lower environmental stress-cracking resistance and lower puncture resistance at low temperature. Compared with lower-flow homopolymers, the grade has a higher melt flow rate, which reduces cycle time and injection pressure but sacrifices some impact strength. These distinctions are most visible in thin-wall applications where material selection is constrained by injection pressure, cooling time and part mass.

    For food-contact and repeated-use packaging, regulatory status is application-specific. Polypropylene homopolymer resins of this composition are generally supported by testing under FDA 21 CFR 177.1520 and EU 10/2011, but the final article must be migration-tested by the converter. Under REACH, the polymer itself is not subject to registration under EC 1907/2006; however, the monomers and additives require registration, and the supplier must confirm that no candidate-list SVHC exceeds 0.1 % w/w in the article. The standard grade does not contain halogenated flame retardants or perfluoroalkyl substances. Specific migration testing under EU 10/2011 must cover fatty, acidic, aqueous and alcoholic simulants as relevant to the intended food type. For repeated-use food containers, the converter must verify residual monomer, additive migration and overall migration against the appropriate food category.

    Standard or regulationDesignationApplicability to PP H1045Verification
    US olefin food-contact resinFDA 21 CFR 177.1520Component of polyolefin articles under listed end-use conditionsLot-specific compliance statement
    EU plastic food-contactEU 10/2011Overall migration and specific migration limitsConverter migration testing
    EU chemicals regulationEC 1907/2006 REACHMonomer and additive registration; SVHC threshold 0.1 % w/wSDS Article 32 declaration
    EU hazardous substances in electronicsDirective 2011/65/EU RoHSRelevant if converted into electrical and electronic equipment componentsSupplier declaration

    Shrinkage of injection-moulded PP H1045 is typically 1.0–2.0 %, depending on wall thickness, gate geometry, packing pressure and cooling layout. A difference between cavity and core coolant temperature above 10 °C produces differential shrinkage and visible warpage in flat lids. Mould temperatures of 10–20 °C reduce sink-mark depth but increase frozen-in orientation and can lower impact at the gate. For dimensionally critical packaging, cooling time should be determined from pressure-volume-temperature data or flow simulation rather than surface solidification alone. Processing aids and colour concentrates with carrier resins of melt flow rate above 100 g/10 min should be evaluated because they can produce anisotropic shrinkage and gate-area appearance defects.

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