Polypropylene Resin PP HP500N

    • Product Name: Polypropylene Resin PP HP500N
    • Factroy Site: Ma'anshan, Ranghulu District, Daqing City, Heilongjiang Province
    • Price Inquiry: sales7@ascent-chem.com
    • Manufacturer: Daqing Refining & Chemical Company
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    Specifications
    HS Code 330310
    Polymertype Polypropylene Homopolymer
    Density 0.90 g/cm³
    Meltflowrate 50 g/10 min (230°C/2.16 kg)
    Tensilemodulus 1600 MPa
    Tensilestressatyield 35 MPa
    Tensilestrainatbreak 15%
    Charpynotchedimpactstrengthat23c 2.5 kJ/m²
    Heatdeflectiontemperatureat0 45mpa 100°C
    Vicatsofteningtemperature 155°C
    Meltingtemperature 165°C
    Moldshrinkage 1.0-2.0%
    Waterabsorption <0.01%
    Electricalvolumeresistivity >10^15 ohm·cm
    Dielectricconstantat1mhz 2.3

    As an accredited Polypropylene Resin PP HP500N factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

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    Application of Polypropylene Resin PP HP500N

    On multi-cavity stack moulds producing lidded household storage articles, PP HP500N with nominal melt flow rate of 5.0 g/10 min per ISO 1133-1:2022 at 230°C/2.16 kg is introduced as the sole polymer matrix at 100.0 parts by weight; opaque-colour masterbatch is let down at 1.5–2.5 wt%, and dust-resistant grades receive an antistatic masterbatch at 1.0–2.0 wt%. The moulding hall humidity boundary is RH 60%; above this value, surface condensation is removed by 80°C forced-air drying for 2.0–3.0 h, with residual moisture held below 0.05 wt%. For food-contact storage articles, compliance is anchored to FDA 21 CFR 177.1520 and Commission Regulation (EU) No 10/2011, with the overall migration limit of 10 mg/dm² and specific migration limits for masterbatch additives according to Annex I. REACH Annex XVII and ISO 19069-2:2016 are used as baseline chemical and specimen-preparation controls when metal inserts are not present. Downstream injection moulding uses hydraulic or servo-electric machines with L/D 20:1–24:1 plasticising screws, barrel set points of 200/210/220/230/230°C and nozzle at 230°C; the mould circuit is held at 20–40°C. Injection velocity is limited to 40–100 mm/s because nucleated homopolymer exhibits rapid skin solidification, and the gate diameter is maintained at 1.0–1.5 mm for wall sections of 1.2–2.5 mm to prevent jetting. Hold pressure is set at 60–80% of peak cavity pressure and cooling time is 8–12 s at 1.2 mm nominal wall. Terminal finished product types include stackable storage crates, drawer organizers, utility boxes, lidded under-bed bins, and dust-resistant archive boxes.

    What Happens to Strip Torque in 28-mm to 38-mm Hinged-Lid Closures at 5.0 g/10 min Melt Flow?

    Closure tools running 5.0 g/10 min nucleated homopolymer at strip torque are constrained by the competition between living-hinge flexural modulus and tamper-evident bridge weld strength. The compounding letdown is 100.0 parts by weight PP HP500N, 2.0–3.0 wt% colour masterbatch, and 0.3–0.8 wt% oleamide/erucamide slip masterbatch to maintain removal torque within 1.0–2.5 N·m for 28–38 mm closures; slip masterbatch exceeding 0.8 wt% is not used because additive bloom alters cap-liner weld adhesion. For food-contact closures, compliance is anchored to FDA 21 CFR 177.1520 and Commission Regulation (EU) No 10/2011, with migration testing performed on the fully assembled closure and liner under Annex III food simulants. The injection line is a 32–64-cavity hot-runner system with valve gates of 0.6–1.2 mm diameter; barrel temperatures are set at 210–240°C, and the mould is held at 15–30°C to set the hinge by fast crystallisation. Melt temperatures above 260°C cause base-resin discolouration, while below 210°C the oriented hinge layer fails to form and whitening appears after flexing. Hinge thickness is set at 0.20–0.35 mm, and the hinge is gated so that flow crosses the hinge transverse to the flexural axis. Injection velocity is 60–120 mm/s, hold pressure 40–70 MPa, and cycle time 8–16 s. The tamper-evident band slitting bridge width is maintained at 0.6–1.0 mm, with slitting-blade rotational speed of 200–400 min⁻¹; blade wear above 0.02 mm radial run-out creates inconsistent bridge break force. Terminal finished product types include 28-mm personal-care flip-top caps, 38-mm spice closures, dry-powder lid sets, and tamper-evident overcaps for food tins. Carbonated-soft-drink pressure closures are outside the intended operational boundary for this grade; internal pressure resistance should be validated for each design.

    Twin-screw compounding operations with co-rotating screws of 40:1 L/D and side feeders located 6–10 barrel diameters upstream of the die plate feed PP HP500N as the 60–90 wt% matrix for filled polypropylene compounds. Talc is metered at 10–40 wt%, calcium carbonate at 10–30 wt%, or chopped glass fibre at 10–20 wt%; maleic anhydride-grafted PP coupling agent is added at 0.3–1.0 wt% to improve filler–matrix interfacial adhesion. Antioxidant masterbatch is added at 0.1–0.3 wt%, and processing aid such as calcium stearate is limited to 0.05–0.15 wt% because higher values reduce fibre–matrix shear transfer. Compliance for automotive compounds is audited against VDA 277:1995 for total volatile organic compounds, VDA 270:2018 for odour, and REACH 1907/2006 SVHC screening; compounds entering electrical applications must comply with RoHS 2011/65/EU. For food-contact compounds, filler and additives must be assessed under Commission Regulation (EU) No 10/2011 Annex I and FDA 21 CFR 177.1520. The melt is processed through barrels set at 180–220°C, with screw speed 400–600 min⁻¹, specific mechanical energy input 0.18–0.25 kWh/kg, an atmospheric vent at 12–16 D, and a vacuum vent at -0.07 MPa to -0.09 MPa; the strand die is held at 220–230°C. Pelletising is conducted with an underwater pelletiser or water-bath at 30–50°C and subsequent classifier density verification to 0.90–1.05 g/cm³ depending on filler content. Published data for exact screw geometry and filler grade are limited; compounding trials must establish filler dispersion with ISO 3451-1:2019 ash content and ISO 180:2023 notched Izod after moulding. Terminal finished product types include appliance back panels, automotive non-visible wheel-arch liners, electrical junction-box covers, battery lids, and garden furniture strips produced from the resulting compound; these components are downstream moulded articles, not direct PP HP500N mouldings.

    Downstream scenarioPrimary chemical or migration controlPrimary mechanical/thermal test methodAdditional regulatory boundary
    Housewares and storage articlesFDA 21 CFR 177.1520; Commission Regulation (EU) No 10/2011 with overall migration 10 mg/dm²ASTM D638-14; ISO 178:2019; ISO 1133-1:2022REACH Annex XVII; metal-insert exclusion unless tested
    Caps and closuresFDA 21 CFR 177.1520; Commission Regulation (EU) No 10/2011 Annex IASTM D638-14; ISO 180:2023; ISO 1133-1:2022REACH SVHC screening; pressure-closure exclusion
    Filled compoundingVDA 277:1995; VDA 270:2018; Commission Regulation (EU) No 10/2011 for food gradesISO 3451-1:2019; ISO 180:2023; ISO 178:2019RoHS 2011/65/EU; REACH SVHC screening
    Laboratory consumablesPh. Eur. 3.1.3; USP <661>; ISO 10993-5:2009ISO 178:2019; ISO 294-4 dimensional controlISO 13485:2016; ISO 14644-1 cleanroom classification
    Appliance componentsIEC 60335-1:2020; RoHS 2011/65/EUISO 178:2019; UL 94 HB at 1.5 mmFire-enclosure revalidation if filler is added
    Industrial pails and containersUN Model Regulations Chapter 6.1; 49 CFR Part 178 for dangerous goodsASTM D790-17; ISO 1133-1:2022; ASTM D257-14REACH 1907/2006; RoHS 2011/65/EU

    Laboratory Consumable Moulding Without Processing-Migration Additives

    Laboratory consumable moulding without processing-migration additives imposes stricter additive-control boundaries than industrial packaging because leachates can interfere with chromatographic and spectroscopic detection. PP HP500N is processed as 100.0 wt% base resin; colour masterbatch is limited to 0.5–1.5 wt% and must be pre-validated against the intended solvent matrix. Slip agents, mould-release agents, and antistatic masterbatches are excluded unless a leachables study demonstrates no interference; if release is required for complex geometries, a medical-grade polydimethylsiloxane-free release agent is used only on the tool surface and validated by extraction testing. Compliance is treated as a quality-system and biological-evaluation problem: moulders supplying diagnostic device manufacturers operate under ISO 13485:2016; articles intended for pharmaceutical contact are tested against Ph. Eur. 3.1.3 and USP <661>; if the article is part of a medical device, ISO 10993-5:2009 cytotoxicity and ISO 10993-1:2018 risk evaluation are required. PP HP500N starting material alone does not establish USP Class VI or ISO 10993 compliance. Production is run on all-electric injection moulding machines with 35–50 mm screw diameter, L/D 20:1–24:1, and chromium-nitride-coated barrels to reduce metal wear particles; melt temperature is 200–230°C, mould temperature 20–40°C, injection velocity 30–80 mm/s, hold pressure 50–70 MPa, and back pressure 0.5–1.0 MPa. Cleanroom classification is ISO 14644-1 Class 8 for non-sterile diagnostic articles and Class 7 for sterile barrier components, with positive pressure differentials of 10–15 Pa. Reclaimed material is limited to 20 wt% for non-diagnostic products and prohibited for pharmaceutical-contact articles. Dimensional stability is checked with ISO 294-4 shrinkage plates under 24 h post-mould conditioning at 23°C/50% RH. Terminal finished product types include specimen transport cups, diagnostic sample vials, petri-dish covers, test-tube racks, and microplate adapters; implantable and blood-contacting devices are outside the verified boundary.

    In refrigerator air-distribution housings and washing-machine detergent dispenser bodies, PP HP500N is processed through 2.0–3.0 mm wall sections in tools that use conformal cooling cartridges to hold sink-mark depth below 0.05 mm. The formulation uses 100.0 parts by weight PP HP500N, 0.5–2.0 wt% colour masterbatch, and 10–20 wt% talc masterbatch only where flexural modulus above 2200 MPa is required; otherwise the moulded part retains neat homopolymer rigidity above 1500 MPa per ISO 178:2019. Compliance is controlled by IEC 60335-1:2020 for household electrical-appliance safety, RoHS 2011/65/EU for restricted substances, and UL 94 HB at 1.5 mm or greater thickness; if the part is a fire enclosure, a V-2 compound is required and the talc masterbatch letdown must be revalidated because filler can alter burning behaviour. Injection moulding is performed on hydraulic machines with 50–80 mm screws, melt temperature 210–250°C, mould temperature 20–40°C, injection velocity 60–120 mm/s, hold pressure 60–80 MPa, and back pressure 0.5–1.0 MPa; screw recovery is maintained at 30–70% of shot capacity to avoid residence-time degradation. Hot-runner manifold temperatures are set at 220–240°C, with gate diameter 1.2–2.0 mm to avoid shear-heating discolouration. Terminal finished product types include refrigerator crisper trays, freezer door bins, washing-machine detergent dispenser housings, lint-filter bodies, and air-conditioner drainage pans.

    Downstream scenarioTypical additive letdown outside PP HP500NMelt temperature windowPrimary process constraint
    Housewares and storage articles1.5–2.5 wt% colour; 1.0–2.0 wt% antistat210–230°CGate diameter below 1.0 mm causes jetting
    Caps and closures2.0–3.0 wt% colour; 0.3–0.8 wt% slip210–240°CHinge whitening below 210°C
    Filled compounding10–40 wt% filler; 0.3–1.0 wt% coupling agent180–220°CVacuum-vent blockage from fines
    Laboratory consumables0.5–1.5 wt% pre-validated colour200–230°CLeachable interference without additive exclusion
    Appliance components0.5–2.0 wt% colour; 10–20 wt% talc only if stiffened210–250°CSink marks on 2.0–3.0 mm walls
    Industrial pails1.0–2.0 wt% colour; 0.2–0.5 wt% UV stabiliser220–250°COvality at lid seat above 1.5% shrinkage differential

    When 10-L Paint Pail Moulds Run Nucleated Homopolymer at 5.0 g/10 min

    When 10-L paint pail moulds run 5.0 g/10 min nucleated homopolymer, the dominant processing risk is differential shrinkage between the thick handle boss and the 2.0–3.0 mm sidewall, which can exceed 1.5% and produces ovality at the lid seat if cooling is non-uniform. The formulation uses 100.0 parts by weight PP HP500N, 1.0–2.0 wt% colour masterbatch, 0.2–0.5 wt% UV stabilizer masterbatch for outdoor exposure, and 1.0–2.0 wt% antistatic masterbatch only for solvent-based filling lines; antistatic migration into water-based paint must be validated by ASTM D257-14 surface resistivity and product-specific stability tests. Dangerous-goods pails are manufactured and tested to UN Model Regulations Chapter 6.1 and 49 CFR Part 178; a 1.2 m drop height for packing group II and the leakproofness test at 30 kPa are the accepted minimum verification points. For non-dangerous paint and adhesive packaging, REACH 1907/2006 and RoHS 2011/65/EU apply. Injection moulding uses a cold-runner direct sprue or hot tip at 2.0–3.0 mm diameter, melt temperature 220–250°C, mould temperature 20–35°C, injection velocity 50–100 mm/s, hold pressure 70–90 MPa, and cooling time 25–40 s at 2.5 mm wall; vents are cut to 0.02–0.03 mm depth to prevent flow-front burns. The handle boss is cored to keep wall-thickness variation below 0.5 mm, and lid-seat roundness is checked with a coordinate measuring machine after 24 h conditioning at 23°C/50% RH. Terminal finished product types include 10-L, 15-L, and 20-L paint pails, adhesive tubs, grease pails, and industrial chemical containers.

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