| HS Code | 386690 |
| Density | 0.90 g/cm³ |
| Melt Flow Rate | 10 g/10min (230°C, 2.16kg) |
| Tensile Strength At Yield | 35 MPa |
| Elongation At Break | 100% |
| Flexural Modulus | 1400 MPa |
| Izod Impact Strength Notched 23 C | 25 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 100 °C |
| Vicat Softening Point | 155 °C |
| Rockwell Hardness | R100 |
| Melting Point | 165 °C |
| Shrinkage | 1.5% |
As an accredited Jinneng PP Homopolymer HP500N factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Jinneng PP Homopolymer HP500N is packaged in 25 kg woven polypropylene bags with inner liner, palletized and shrink-wrapped. |
| Container Loading (20′ FCL) | 20' FCL: Polypropylene homopolymer HP500N packed in 25kg bags on pallets, secured with shrink wrap, loaded weatherproof. |
| Shipping | Ship as polypropylene homopolymer resin in clean, dry railcars, trucks, or ocean containers. Protect from moisture, heat, and direct sunlight to prevent degradation. Keep bags or bulk units intact and well-ventilated. No hazardous classification applies, but avoid airborne dust accumulation and handle with standard industrial hygiene practices. |
| Storage | Store Jinneng PP Homopolymer HP500N 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. Avoid contact with strong oxidizers. Use proper grounding to prevent static discharge. Maintain room temperature; do not stack excessively high. Protect bags from damage during handling. |
| Shelf Life | Store in a cool, dry place away from sunlight and moisture. Shelf life is typically two years from date of manufacture. |
Within thin-wall injection moulding cells producing rigid polypropylene food-service articles, Jinneng PP Homopolymer HP500N is specified as the primary virgin resin where melt stability under high shear and rapid solidification are governing criteria. The production route is high-speed injection moulding on accumulator-assisted machines with clamp force from 1,800 kN to 6,500 kN and plasticating units having L/D ratios of 22:1 to 25:1; melt temperature is maintained between 220°C and 250°C, mould temperature is controlled from 10°C to 30°C, and injection velocity is set above 250 mm/s for wall sections between 0.35 mm and 0.8 mm. A recurring failure mode in this geometry is premature freeze-off at valve-gate tips when injection pressure exceeds 120 MPa at the lower melt-temperature boundary, producing flow hesitation lines on sidewall regions thinner than 0.6 mm; this is corrected by raising holding pressure from 30 MPa to 50 MPa and increasing gate diameter until pressure drop across the gate is less than 35 MPa at the maximum injection velocity. Rheological lot acceptance uses ISO 1133-1:2022 at 230°C and 2.16 kg; converters should verify shipment-specific MFR against tool-filling simulation results before cutting steel.
HP500N constitutes 97.5–99.5 wt% of the compound. A nucleating agent masterbatch is introduced at 0.05–0.20 wt% to elevate crystallization temperature and shorten cooling time; slip/antiblock masterbatch is added at 0.5–1.5 wt% where denesting force below 15 N per container is required. No plasticizer, phthalate, or bisphenol-A source is required in an olefin homopolymer formulation. Clean post-industrial regrind is incorporated up to 20 wt% only after migration and impact validation; post-consumer recyclate is excluded from direct food-contact layers under EU Regulation (EU) 2022/1616 unless the specific recycling process is authorized.
Food-contact compliance is assessed under EU Regulation 10/2011 as amended by (EU) 2020/1245 with overall migration limited to 10 mg/dm² in aqueous, acidic, and fatty simulants. U.S. market acceptance references FDA 21 CFR 177.1520(c) 1.1 for olefin polymers, and the Chinese compliance reference is GB 4806.6-2016. A supplier declaration under REACH 1907/2006 Article 33 is expected for SVHC content above 0.1 wt%, though olefin homopolymer grades normally do not require phthalate or heavy-metal alerts under standard catalyst systems. Terminal finished article types include dairy cups in 120–250 ml formats, delicatessen containers, tamper-evident food pails, and food-service trays with rim-to-wall transitions designed for stacking and lidding.
A single-piece beverage closure combines tamper-evident band, primary sealing bore, and living hinge; HP500N is evaluated in this geometry for torque retention and hinge endurance after everted band application. In 24- to 96-cavity hot-runner tools, the material is processed at melt temperature 230–250°C and mould temperature 15–30°C; injection pressure ranges from 80 MPa to 110 MPa, holding pressure from 35 MPa to 55 MPa, and cycle time from 6 s to 12 s. Stress whitening at the hinge is observed when the part is ejected at hinge temperature above 80°C or when the hinge thickness exceeds 0.35 mm and stiffness concentrations are not relieved by a radius above 0.2 mm; delayed hinge ejection of 0.2–0.8 s reduces oriented skin rupture and improves flexural endurance. Published data for this specific grade in clarified high-gloss closure compounds is limited; haze and torque retention must be confirmed on the production tool.
Formulation for closure systems uses HP500N at 96.0–99.0 wt%, slip agent masterbatch at 0.05–0.15 wt%, acid scavenger at 0.02–0.05 wt%, and optional peroxide-controlled vis-breaking only when mould-filling and drop-impact requirements have been jointly satisfied. Higher slip levels above 0.2 wt% can exude to the sealing bridge and lower removal torque below 1.0 N·m, which is generally outside the commercial window for carbonated soft drink closures after 7 days at 38°C.
Food-contact closure compliance uses EU Regulation 10/2011 with overall migration 10 mg/dm², FDA 21 CFR 177.1520(c) 1.1, and China GB 4806.6-2016; pharmaceutical closure validation may require USP Chapter 661.1 and Ph Eur 3.1.3 polyolefin monographs, which are end-application validations and are not automatically satisfied by resin compliance alone. Finished article types include still-water closures, carbonated soft drink closures, tamper-evident pharmaceutical closures, cosmetic flip-top caps, and child-resistant closures after secondary ratchet or insert assembly.
When a non-plated internal housing must retain dimensional stability after repeated thermal cycling in a small home appliance, HP500N is compared against talc-filled compounds and lower-MFR polypropylene homopolymer grades. The unfilled injection-moulding grade is selected where flexural modulus above 1,300 MPa is sufficient, heat deflection temperature under 0.45 MPa is above 90°C, and notched Charpy impact above 4 kJ/m² at 23°C is acceptable. The production process is conventional single-stage injection moulding with clamp force from 1,200 kN to 5,000 kN, melt temperature 210–240°C, mould temperature 20–50°C, and holding pressure profiles from 40 MPa to 65 MPa. Screw recovery speed is limited to 80–150 rpm to avoid excessive shearing at thin ribs; inadequate screw recovery can increase short-shot occurrence. Continuous exposure to water above 80°C under stress should be excluded due to creep and detergent-assisted oxidation.
HP500N is dosed at 96.0–99.0 wt% with a primary/secondary antioxidant package at 0.05–0.15 wt%, acid scavenger at 0.02–0.05 wt%, and optional antistatic masterbatch at 0.2–0.8 wt% where dust attraction on control panel surfaces is a concern. The base grade does not include a flame-retardant package; flammability classification for unfilled polypropylene is normally UL 94 HB at 1.5 mm and 3.2 mm, and V-0 classification cannot be presumed without a flame-retardant compound.
Compliance requires IEC 60335-1:2020 end-product testing for household electrical appliances, including abnormal heat and glow-wire provisions where applicable; material-level mechanical data are evaluated under ISO 178:2019, ISO 527-1:2019, ASTM D638-14, and ASTM D790-17. RoHS compliance is verified under Directive 2011/65/EU and REACH under REACH 1907/2006; no halogenated flame retardant is required in HB applications. Terminal finished parts include washing machine top panels, air-conditioner drain pans, vacuum cleaner housing components, small appliance bases, and dishwasher spray-arm supports where short-term hot-water contact remains below 80°C.
In returnable logistics moulding, HP500N is compounded with hindered-amine light stabilizers rather than benzotriazole-only packages to retain impact strength after outdoor storage. The process is low-pressure structural injection moulding, using clamp force from 8,000 kN to 25,000 kN for pallet boxes and 1,500 kN to 5,000 kN for crates and totes; melt temperature is held at 220–250°C, mould temperature at 15–40°C, injection pressure at 70–100 MPa, and holding pressure at 30–55 MPa. Gas-assisted injection is applied for thick ribs above 6 mm to core the section and reduce sink marks; without gas assist, sink defects occur at intersections with wall thickness differences greater than 3:1.
HP500N forms 97.0–99.5 wt% of the compound; UV stabilizer masterbatch is introduced at 0.15–0.50 wt%, antioxidant at 0.05–0.10 wt%, and optional nucleating agent at 0.05–0.10 wt% for uniform demoulding. High-load logistics applications may use talc-reinforced versions only if the base resin is compounded at 70–90 wt% with talc masterbatch 10–30 wt%, but such compounds lie outside the unfilled HP500N grade and require separate weld-line validation.
Mechanical compliance uses ISO 179-1:2020 Charpy notched impact at 23°C; the material is not recommended for continuous cold-store service below -10°C without notched-impact validation because brittle failure can occur under dropping at -20°C. Pallet-type units are tested under ISO 8611-1:2021 for end-product load performance; crates and totes are stack-load tested according to customer-specific compression and drop standards because no single ISO standard covers all geometries. RoHS and REACH compliance is stated under Directive 2011/65/EU and REACH 1907/2006. Terminal finished article types include folding crates, dairy crates, bread trays, logistics totes, and pallet boxes with optional anti-slip grommets or RFID pockets moulded into the sidewall.
Melt cleanliness and batch-to-batch flow consistency determine whether a homopolymer PP grade is accepted for non-optical laboratory consumable tooling. For diagnostic device housings and specimen transport containers, HP500N is processed on reciprocating-screw injection machines with barrel temperatures from 210°C to 240°C, mould surface temperatures between 20°C and 45°C, and holding pressures from 30 MPa to 55 MPa. The critical production control is avoidance of cross-contamination in shared equipment; dedicated hoppers and purge procedures with low-MFR polyolefin purge compound are used after PVC or ABS colour changes, because even 0.1 wt% carry-over can produce delamination or contamination-derived cytotoxicity failures.
HP500N is used at 99.0–99.8 wt%; the additive package is limited to antioxidant at 0.02–0.10 wt% and nucleating agent at 0.05–0.15 wt% where consistent cycle-time and shrinkage are required. Slip agents and antiblock are omitted unless part denesting or handling demands them; any additive used in a laboratory or diagnostic application must be disclosed on the material declaration for biocompatibility review.
Regulatory requirements are not uniform across all laboratory consumables. Non-implant diagnostic enclosures and specimen transport articles may be evaluated under ISO 10993-1:2018 biological risk management and ISO 10993-5:2009 cytotoxicity; pharmaceutical packaging contact may require USP Chapter 661.1 and Ph Eur 3.1.3; food-contact disposables remain under FDA 21 CFR 177.1520(c) 1.1 and EU Regulation 10/2011. Repeated steam autoclaving at 121°C under load is not recommended because the grade has heat deflection temperature under 0.45 MPa near 90°C; unloaded cycles may be acceptable but dimensional change and part sticking should be validated. Terminal finished article types include diagnostic device enclosures, specimen transport cups, laboratory tray racks, non-optical disposable scoops, and small benchtop equipment housings.
Under-hood HVAC components manufactured from HP500N are typically free of short glass fiber to reduce tool wear and mass; unfilled sections are specified where the service temperature remains below 100°C, while talc-filled flow paths are selected for duct walls requiring higher modulus. Injection moulding uses clamp force from 3,000 kN to 12,000 kN, melt temperature 220–250°C, mould temperature 30–60°C, injection speed 80–180 mm/s, and holding pressure 35–60 MPa. Weld lines at air-outlet ribs and mounting bosses are failure-prone zones; if vent depth is less than 0.02 mm or if melt temperature falls below 220°C, Charpy impact at the weld line can drop by more than 30% relative to the base resin, and burn streaks may appear on the parting line.
HP500N is the base resin at 70–95 wt%; talc masterbatch is compounded at 5–30 wt% for stiff duct walls and air-filter frames, antioxidant/heat stabilizer at 0.10–0.30 wt%, and optional carbon black at 0.2–0.8 wt% for UV shielding in engine-compartment ambient exposure. If olefin-based impact modification is needed, the formulation moves toward a copolymer system; HP500N itself remains the high-flow homopolymer baseline for mould filling and dimensional consistency.
Automotive material compliance uses FMVSS 302 and ISO 3795:1989 flammability for occupant compartments, ISO 6452:2021 fogging gravimetric or reflectometric methods, and OEM-specific odour and VOC standards such as VDA 270 and VDA 277. Published data for this specific grade in under-hood thermal ageing beyond 1,000 h at 120°C is limited; validation on the actual component is required. Terminal finished part geometries include HVAC air ducts, heater housings, fan shrouds, air-filter housings, and resonator shells.
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Jinneng PP Homopolymer HP500N is a medium-flow polypropylene homopolymer supplied for injection molding of opaque or colored durable goods and packaging components. The product model HP500N identifies a reactor-grade isotactic polypropylene without ethylene comonomer or dispersed rubber phase. The grade is characterized by a nominal melt flow rate of 12 g/10 min at 230 °C and 2.16 kg load under ISO 1133-1:2022, with a density of 0.90 g/cm³ under ISO 1183-1:2019. The resin is supplied as cylindrical pellets with ash content commonly controlled below 0.03 wt% under ISO 3451-1:2019. The material is neither a clarified random copolymer nor an impact-modified reactor blend, and this architecture determines its stiffness, thermal resistance, and low-temperature impact ceiling. The primary usage envelope includes caps, closures, houseware components, appliance trim, storage containers, and thin-wall packaging where stiffness, dimensional control, and cycle-time stability are required.
The medium-flow position of HP500N is defined by a melt mass-flow rate window of 10 g/10 min to 14 g/10 min at 230 °C under 2.16 kg, with typical lot data near 12 g/10 min. This value places the grade below high-flow homopolymers that reach 25 g/10 min or higher and above extrusion-oriented grades that operate below 3 g/10 min. High-flow variants fill thin sections at lower injection pressure, but the molecular weight reduction that produces high flow also lowers notched impact strength and tensile yield stress. HP500N retains sufficient melt viscosity to limit gate stringing and sink marks in section thicknesses above 2.0 mm, while still permitting wall thickness down to 0.8 mm when gate geometry and pack pressure are designed for fast filling. The medium-flow specification therefore shifts process risk from mold filling to packing and shrinkage control, producing lower short-shot frequency in thick bosses and higher sensitivity to gate seal time.
On injection molding machines with general-purpose screws of 20:1 to 25:1 L/D and compression ratios of 2.5:1 to 3:1, melt temperatures are commonly set between 200 °C and 250 °C. A typical four-zone barrel profile from feed throat to nozzle is 180 °C, 200 °C, 220 °C, and 230 °C, with hot-runner manifold temperatures not exceeding 240 °C and nozzle tip temperature held at 230 °C to 235 °C. Mold temperatures are maintained at 20 °C to 50 °C; increasing mold temperature toward 50 °C increases crystallinity and flexural modulus but extends cooling time and raises shrinkage anisotropy. Injection pressure is tool-dependent and generally falls between 60 MPa and 120 MPa. Holding pressure is set at 70% to 80% of peak injection pressure. Screw rotation speed is typically 30 rpm to 80 rpm with a back pressure of 0.5 MPa to 1.5 MPa. The material does not require mandatory drying when granule moisture remains below 0.05 wt%. If storage relative humidity exceeds 60%, a desiccant hopper dryer operating at 80 °C for 2 h to 4 h with a dew point below -20 °C prevents surface splay and additive hydrolysis.
A process window restriction appears in hot-runner systems with gate diameters below 0.8 mm. High injection velocity can generate shear heating that raises local melt temperature above 270 °C, causing oxidative chain scission, yellowing, and black speck formation. Shrinkage anisotropy is a significant conversion variable in HP500N. Flow-direction shrinkage is typically 1.4% to 1.7%, and cross-flow shrinkage can be 0.1% to 0.3% higher depending on gate type and packing time. The difference in shrinkage vectors drives warpage in rectangular parts. A long packing-pressure profile at 70% to 80% of peak pressure for 6 s to 12 s in a 2 mm wall reduces orientation-induced differential shrinkage, but it increases cycle time. In multi-cavity tools with naturally balanced melt paths, cavity-to-cavity weight variation should be held below 0.5%; above that threshold, flash or short shot appears in the outer cavities.
The values in the following table are representative lot data for unfilled homopolymer polypropylene, not minimum sales specifications. Specimens for tensile and flexural evaluation are injection molded according to ISO 294-1:2017, conditioned at 23 °C and 50% RH for 40 h, and tested at 50 mm/min under ISO 527-2:2012 for tensile yield stress and at 2 mm/min under ISO 178:2019 for flexural modulus. Notched Izod impact uses type A notches under ISO 180/A:2023.
| Property | Test method | Typical value or range |
|---|---|---|
| Density | ISO 1183-1:2019 | 0.90 g/cm³ |
| Melt flow rate, 230 °C/2.16 kg | ISO 1133-1:2022 | 10–14 g/10 min |
| Tensile yield stress | ISO 527-2:2012 | 34–36 MPa |
| Tensile elongation at yield | ISO 527-2:2012 | 9–12% |
| Flexural modulus | ISO 178:2019 | 1450–1550 MPa |
| Notched Izod impact, 23 °C | ISO 180/A:2023 | 2.8–3.2 kJ/m² |
| Notched Izod impact, -20 °C | ISO 180/A:2023 | 1.5–2.0 kJ/m² |
| Vicat softening temperature, A50 | ISO 306:2022 | 153 °C |
| Heat deflection temperature, 0.45 MPa | ISO 75-2/B:2013 | 96 °C |
| Mold shrinkage, longitudinal | ISO 294-4:2018 | 1.4–1.7% |
Heat deflection at the higher stress of 1.8 MPa under ISO 75-2/A:2013 is typically 55 °C to 60 °C. These thermal values explain why HP500N is unsuitable for under-hood automotive parts above 90 °C continuous air temperature unless the part is unstressed or the exposure duration is short. The notched Izod values at -20 °C define the low-temperature limit: HP500N should not be used in impact-critical components that experience sub-zero drop loading, because failure occurs by brittle fast fracture rather than ductile yielding. The Vicat softening temperature of 153 °C does not indicate continuous use temperature. Polypropylene homopolymer under sustained mechanical load oxidizes above 80 °C to 90 °C unless stabilized for long-term heat aging. Applications that expose HP500N to hot water, steam, or air above 100 °C require additional heat-stabilization packages and should be validated by oven aging per ISO 4577:2019 or ASTM D3012-19.
Random copolymer grades are selected when clarity and low-temperature ductility are primary requirements. HP500N is substituted when the part is opaque or colored, wall thickness is below 1.2 mm, and the controlling conversion variable is demolding stiffness. Without ethylene comonomer interrupting the polypropylene chain, the crystallization rate and spherulite nucleation behavior of HP500N produce a flexural modulus of 1450 MPa to 1550 MPa, compared with 800 MPa to 1050 MPa for typical random copolymers in the same melt-flow band. This stiffness allows earlier ejection without wall distortion and permits down-gauging in thin-wall lids, dairy cups, and disposable food containers. The trade-off is a loss of contact clarity and lower puncture energy at refrigerator temperatures. When a product specification includes a haze target below 5% on a 1 mm plaque under ASTM D1003-21, HP500N is not the appropriate choice.
The base homopolymer is not formulated with heavy-metal pigments, ortho-phthalate plasticizers, or halogenated flame retardants. Food-contact suitability for uncolored, unfilled HP500N can be evaluated under FDA 21 CFR 177.1520 for olefin polymers, GB 968.5-2016 for polypropylene food-contact materials, and EU Regulation (EU) No 10/2011 with a finished-article overall migration limit of 10 mg/dm² when tested under the specified food simulants and time/temperature conditions. Compliance under REACH and RoHS Directive 2011/65/EU depends on the finished compound and the converter’s supply chain, but the base resin does not intentionally contain cadmium, lead, mercury, or hexavalent chromium above the threshold of 100 ppm.
Impact copolymer grades containing an ethylene-propylene rubber phase are selected when notched Izod impact at -20 °C must exceed 5 kJ/m². HP500N falls between 1.5 kJ/m² and 2.0 kJ/m² in that test. In appliance housings, power-tool bodies, luggage shells, and reusable crates that must survive cold drop events, impact copolymers provide a larger fracture-energy safety margin. HP500N is selected for room-temperature service with a dominant stiffness requirement, such as appliance trim, enclosure bases, and storage components that must resist wall deflection under compressive stack load. The high modulus of HP500N also reduces creep strain under load at 23 °C compared with random copolymers, but creep rupture data on this specific grade are limited and should be generated for continuously loaded parts using ISO 899-1:2017.
| Comparative property | HP500N homopolymer | Random copolymer class | Impact copolymer class |
|---|---|---|---|
| Flexural modulus | 1450–1550 MPa | 800–1050 MPa | 1100–1400 MPa |
| Notched Izod at 23 °C | 2.8–3.2 kJ/m² | 4.0–6.0 kJ/m² | 10–30 kJ/m² |
| Notched Izod at -20 °C | 1.5–2.0 kJ/m² | 1.5–2.5 kJ/m² | 5.0–8.0 kJ/m² |
| Vicat softening, A50 | 153 °C | 130–145 °C | 145–155 °C |
| Optical character | opaque/translucent | clear in thin sections | opaque |
Comparative figures are category benchmarks; specific grades and producer certificates vary. Weld lines in HP500N are more damaging than in impact-copolymer grades because the homopolymer lacks a dispersed rubber phase to bridge meeting fronts. In ribbed or bossed sections with weld lines, tensile strength retention is typically 60% to 70%. Gate placement should move weld lines into low-stress areas, and melt temperature should be kept between 230 °C and 240 °C to improve front knitting.
Barrel residence time at 230 °C should be kept below 15 min, and the cushion should be controlled between 4 mm and 6 mm. When a downstream fault stops the press, screw rotation should be stopped and barrel zone temperatures reduced by 20 °C if the interruption exceeds 10 min. Regrind from sprues, runners, and rejected parts can be reintroduced into HP500N at levels of 10 wt% to 20 wt% in non-color-critical applications without additional stabilizer extension. Above 30 wt% regrind, repeated heat history raises melt flow rate by 2–5 g/10 min per pass and lowers notched impact strength. Regrind should be ground with a screen size below 8 mm and conveyed with granule temperature below 50 °C to prevent pellet bridging in the feed throat. If flame-retardant masterbatches are required, halogenated systems based on antimony trioxide may need adhesion promoters because of the nonpolar surface of polypropylene; non-halogen intumescent packages can increase melt pressure and should be tested for screw torque limits.
For a multi-cavity hot-runner cap tool, the injection speed profile is typically split into a high-velocity filling phase of 100–140 mm/s and a pack phase of 30–50 mm/s. The switch-over from velocity to pressure control is selected after 90% of the cavity volume is filled; early switch-over produces short shots in the gate vicinity, while late switch-over raises cavity pressure above 60 MPa and increases flash and ejection force. Applied sidewall draft angles of 0.5° to 1.0° and consistent mold surface preparation reduce ejection-force spikes. Batch-to-batch differences in melt flow rate within the 10 g/10 min to 14 g/10 min window are compensated by adjusting barrel zone temperatures by ±5 °C rather than altering injection velocity. In high-speed packaging machines with cycle times below 8 s, the gate-freeze time for a 0.8 mm wall is the critical control parameter; pack pressure must be maintained until the gate reaches the freezing condition, otherwise sink marks form on the outer surface of the cap skirt.