| HS Code | 604422 |
| Density | 0.90 g/cm³ at 23°C |
| Melt Flow Rate | 12 g/10min at 230°C/2.16kg |
| Tensile Stress At Yield | 35 MPa |
| Tensile Strain At Yield | 10% |
| Flexural Modulus | 1600 MPa |
| Charpy Notched Impact Strength At 23 C | 3.0 kJ/m² |
| Rockwell Hardness | R 100 |
| Heat Deflection Temperature | 100°C at 0.45 MPa |
| Vicat Softening Temperature | 155°C at 50 N |
| Melting Temperature | 165°C |
| Mold Shrinkage | 1.5-2.5% |
| Electrical Resistivity | >10^15 Ω·cm |
As an accredited MOPLEN PP HP500N factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | MOPLEN PP HP500N polypropylene homopolymer is packaged in 25 kg multi-ply paper bags, palletized and wrapped for safe transport and storage. |
| Container Loading (20′ FCL) | 20′ FCL container loading of MOPLEN PP HP500N polypropylene resin, in 25kg bags on pallets, safe, dry, and secure. |
| Shipping | MOPLEN PP HP500N is a non-hazardous polypropylene homopolymer supplied as solid granules. Ship in clean, dry containers or bags, avoiding moisture and direct heat. No special transport classification required under ADR/IMDG/IATA, though standard protection against contamination and physical damage is recommended. |
| Storage | Store Moplen PP HP500N in a cool, dry, well-ventilated area, away from direct sunlight, heat, and open flames. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid stacking bags excessively high to prevent damage. Maintain good housekeeping to minimize dust accumulation. No special temperature control is required, but protect from extreme heat and humidity. |
| Shelf Life | Store in original sealed packaging in dry, cool conditions, away from direct sunlight. Shelf life is typically one year from delivery. |
High-cavitation molds for thin-wall dairy cups and deli containers running MOPLEN PP HP500N require melt-flow consistency within ±2% MFR drift across lot-to-lot deliveries. The nominal melt flow rate of 12 g/10 min measured under ISO 1133-1 at 230 °C and 2.16 kg permits filling of wall sections from 0.40 mm to 0.80 mm at flow-to-thickness ratios exceeding 200:1 in cold-runner tools. In production, a nozzle melt-temperature envelope of 220 °C to 250 °C is maintained; below 220 °C, frozen-layer growth in the cavity reduces the effective flow channel and produces short shots in the rim stack, while above 250 °C, residence-time degradation in hot-runner manifolds causes plate-out and yellowing. Hold pressure is set at 55% to 70% of peak injection pressure and applied for 0.6 s to 1.2 s to suppress sink marks around stacking rims without overpacking the gate vestige. Mold temperature is typically 15 °C to 30 °C; lower settings shorten cycle time but raise residual hoop stress and split-propagation tendency in drop tests. No impact modifier is blended for these applications; converters dose 2% to 4% white masterbatch or a custom PP carrier color concentrate, and the mixture is fed through a gravimetric dosing unit at the throat. Food-contact compliance rests on US FDA 21 CFR 177.1520 for olefin polymers and EU Regulation 10/2011 with overall migration limits of 10 mg/dm² determined under EN 1186 using 3% acetic acid and 10% ethanol simulants for acidic and fatty food contact. Terminal products include 500 mL yoghurt cups, 250 g margarine tubs, and hinged delicatessen containers with walls between 0.45 mm and 0.8 mm. On multi-cavity fast-cycle production cells with toggle clamps typically in the 250 t range, cavity mass variation above 1.5% leads to inconsistent lid-closure force in downstream filling lines; balanced valve-gated hot runners with gate diameters of 0.8 mm to 1.2 mm are used to keep fill imbalance below 3%. Core-temperature drift exceeding ±2 °C across the mold face induces rim warpage that can reach 0.5 mm, which causes seal failure in ultrasonic or friction-fit lidding.
Closure manufacturers running still-water, dairy, and non-carbonated beverage cap programs use the 12 g/10 min MFR of HP500N to fill narrow tamper-evident band walls of 0.35 mm to 0.60 mm in 32- to 64-cavity tools without melt fracture, provided nozzle temperature is kept between 225 °C and 245 °C. In high-speed injection molding, the resin is typically dosed with 0.5% to 1.0% erucamide slip masterbatch and 1% to 2% white masterbatch; the slip additive migrates over 24 h to 72 h post-molding and reduces application/removal torque variability. Pre-blending is performed by low-shear screw mixers rather than intensive twin-screw compounding to avoid frictional heat and early additive loss. Mold temperature is held at 10 °C to 20 °C, and high coolant flow keeps cavity surface temperature variation below ±2 °C. This window prevents slit-band post-molding shrinkage, which is measurable as band ovality above 0.3 mm and causes tearing during cap rectification. Above 245 °C melt temperature, the thin band chars at the gate perimeter and creates stress concentrators; below 225 °C, weld lines at the bridge side remain underpacked and produce vertical cracks during ejection. The homopolymer structure of HP500N is not recommended for carbonated soft-drink closures, because the required environmental stress-cracking resistance under CO2 pressure and applied closure torque is better served by clarified random copolymer PP grades; published data for this specific HP500N configuration in carbonated systems is limited. Terminal products include tamper-evident still-water caps, dairy caps with foil-seal retention beads, and non-carbonated isotonic drink closures. In-line quality checks on 48-cavity systems include bridge-thickness gauging at 0.40 mm ± 0.02 mm and cap-weight control with a ±0.5% tolerance, because weight variation above this level shifts the application torque curve beyond the filling-line setpoint.
For deep-draw storage crates, drawer housings, and logistics boxes with nominal wall thickness from 1.5 mm to 3.0 mm, HP500N is processed at lower injection pressure than polypropylene grades with MFR below 6 g/10 min. In these non-appearance, long-flow applications, melt temperature is set between 210 °C and 230 °C, with mold temperature held between 20 °C and 40 °C to balance warpage and surface gloss. Injection speed is profiled from 60 mm/s to 120 mm/s at the screw, and hold pressure is limited to 35% to 50% of peak pressure because thick rib intersections at the crate bottom remain molten for more than 20 s and are prone to overpacking splay. Regrind addition for visible storage parts is generally held at or below 20% by weight; higher levels increase flow variance and generate black specks from degraded melt film on barrel walls, particularly in machines with general-purpose 20:1 L/D screws. The notched Izod impact strength of HP500N at 23 °C is approximately 2.0 kJ/m² to 2.5 kJ/m² under ISO 180/A; therefore crates intended for manual handling in cold-storage environments should be drop-tested at 0 °C to 5 °C, because homopolymer PP undergoes a ductile-to-brittle transition and sidewall ribs can crack at stacking corner impacts. For food-adjacent storage crates used in dry grocery logistics, the same olefinic compliance as food contact, US FDA 21 CFR 177.1520 and EU 10/2011, is typically required by the end specifier even though the crate itself may not directly contact fatty food. Terminal components include stackable banana crates, industrial parts bins, drawer frames, and collapsible logistics boxes with shot weights from 350 g to 1.2 kg.
Dishwasher detergent dispenser housings and washing-machine additive drawers are molded from HP500N because the unfilled homopolymer offers adequate resistance to alkaline detergent media at concentrations up to 5% and temperatures up to 70 °C under intermittent exposure. The unfilled melt at 12 g/10 min MFR fills thin hinge webs and snap-fit tabs in multi-cavity tools at nozzle temperatures between 225 °C and 240 °C. Mold temperature is controlled at 20 °C to 35 °C; lower mold temperatures create visible jetting on the dispenser flanks, while higher mold temperatures extend cycle time without measurable improvement in chemical resistance. In these parts, HP500N is typically colored with 2% to 3% TiO₂ masterbatch, and no impact modifier is added. Short-term heat resistance is defined by the ISO 75-2/B deflection temperature of approximately 90 °C at 0.45 MPa, which provides a functional margin above the 70 °C maximum water temperature in European dishwasher programs. Chemical exposure is validated by immersion in 1% aqueous alkaline detergent solution at 60 °C for 48 h; visual inspection checks for stress whitening at weld lines around the latch boss. The low moisture absorption of HP500N means predrying is generally not required if silo storage is below 60% relative humidity; surface condensation on cold pellets introduced directly from outdoor silos is a more frequent cause of silver streaks in such parts than true pellet moisture. Thin ribs below 0.8 mm in the detergent drawer lid should be vented with 0.02 mm to 0.03 mm land depths to prevent gas burn at the end of fill. Terminal products include dishwasher detergent dispenser housings, washing-machine softener drawers, and steam-iron water tank housings where service temperatures remain below 80 °C.
Diagnostic and laboratory consumable molding limits are set by the translucent nature of HP500N homopolymer, which is acceptable for specimen transport containers, cap closures, and test-tube racks but is not a direct substitute for transparent clarified PP in optically read microplates. Molding conditions for multi-cavity labware tools differ from packaging in that no slip agents or mold-release additives are usually permitted, because these compounds can interfere with surface chemistry in diagnostic assays. The resin is injected at melt temperatures from 215 °C to 230 °C; mold temperature is 20 °C to 30 °C. Ejector pin marks and gate vestiges are controlled to below 0.1 mm protrusion to prevent collection of biological residue. Medical applications require the converter to validate finished part biocompatibility under ISO 10993-1:2018; the base resin data sheet alone does not constitute a medical certification. Sterilization compatibility is typically assessed for ethylene oxide and gamma irradiation. Gamma irradiation at doses above 25 kGy induces measurable embrittlement in homopolymer PP by chain scission and subsequent oxidative degradation; published data for the specific HP500N additive package under 50 kGy is limited, so terminal radiation validation is required for each part geometry. Ethylene oxide cycles with aeration at 50 °C to 55 °C for 12 h to 48 h are generally compatible, but residual solvents must be checked under ISO 10993-7:2008. Terminal components include non-implant specimen transport tubes, centrifuge-tube closure shells, test-tube racks, and analyzer waste containers. For applications requiring subzero impact after storage at -40 °C, the grade should be qualified with notched Izod data under ISO 180/A and not assumed equivalent to impact-modified PP.
Because toy and stationery OEMs increasingly specify non-phthalate, non-PVC olefins for injection-molded components, HP500N is used in rigid toy parts such as building-block shells, pencil-sharpener housings, and document-clip bases. The material contains no ortho-phthalate plasticizers as polymerized; converters must still verify color masterbatch compliance with EU REACH Annex XVII entries for restricted phthalates and with US CPSC children’s product limits. Melt temperature is held between 210 °C and 230 °C to reduce the risk of thermal degradation products that could affect toy odor; mold temperature from 20 °C to 30 °C is used. For toy applications sold in the European Union, the finished article is tested under EN 71-1 for mechanical and physical properties and EN 71-3 for migration of 19 elements, with limits set in the directive. In the United States, ASTM F963 and US 16 CFR Part 1250 are invoked. Production experience shows that gate blush on flat building-block side surfaces is the primary visual defect; it is controlled by placing fan gates with a minimum width of 3.0 mm at the base of the block and by limiting injection speed below 110 mm/s at the screw. Terminal products include rigid toy blocks, construction-set beams, writing-instrument bodies, and filing accessories. Impact-modified grades are substituted if drop tests at 0 °C result in visible cracks; HP500N in thick sections above 2.5 mm is more likely to fail sharp-corner drop tests than random copolymer or block copolymer PP.
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MOPLEN PP HP500N is a nucleated polypropylene homopolymer injection-moulding grade supplied within the LyondellBasell Moplen product line. Producer technical documentation identifies a nominal melt flow rate of 12 g/10 min determined at 230 °C under a 2.16 kg piston load according to ISO 1133-1:2022. Solid-state density is reported as 0.900 g/cm³ under ISO 1183-1:2019. The polymer backbone contains no ethylene comonomer. A nucleating additive package increases crystallisation temperature and refines spherulite size, which raises flexural modulus, reduces haze in thin-wall mouldings, and shortens solidification time relative to a non-nucleated homopolymer of equivalent melt flow rate. Because no discrete elastomer phase is present, low-temperature fracture resistance is governed by matrix yield and craze resistance rather than rubber-phase cavitation; the grade is therefore specified for rigid, dimensionally stable articles rather than sub-zero impact service.
Substitution decisions involving this product require three comparisons. A non-nucleated homopolymer with the same nominal melt flow rate typically shows coarser spherulitic morphology, lower stiffness, and higher haze under identical moulding conditions. A random copolymer containing 2 wt% to 4 wt% ethylene comonomer possesses lower flexural modulus and lower heat deflection temperature but improved impact strength and optical clarity. An impact copolymer introducing a discrete ethylene-propylene rubber phase provides greater low-temperature ductility while reducing modulus and increasing the potential for mould deposit during prolonged production campaigns. These differences are process-dependent, and the producer’s lot-specific certificate of analysis should be referenced before any grade interchange.
Nucleation alters the solidification behaviour observed under differential scanning calorimetry. In a nucleated homopolymer, the crystallisation exotherm shifts to higher temperature, and the half-crystallisation time decreases because the nucleating agent provides a large number of heterogeneous nucleation sites. The resulting morphology contains smaller spherulites, which scatter visible light less strongly and produce lower haze in solidified plaques. Haze is typically assessed on 1 mm injection-moulded specimens according to ASTM D1003 or ISO 14782; exact values depend on mould polish, melt temperature, and additive package. Flexural modulus measured under ISO 178:2019 is higher than that of a non-nucleated homopolymer of similar melt flow rate because smaller spherulites reduce the scale of weak boundaries and increase load transfer through the semicrystalline matrix.
Random copolymer grades differ in chain architecture. The incorporation of ethylene units interrupts polypropylene crystallinity and lowers the modulus, yield stress, and heat deflection temperature. In exchange, the random copolymer improves impact toughness and optical transparency. MOPLEN PP HP500N is not a sealing resin; its higher melting temperature and absence of ethylene make it less suitable for heat-seal layers, where a random copolymer with a lower seal initiation temperature is preferred. For cap and closure applications, however, the homopolymer’s higher tensile strength and creep resistance support dimensional stability on a closure thread under sustained top load.
The melt flow rate of 12 g/10 min under ISO 1133-1:2022 places MOPLEN PP HP500N in the medium-flow segment of injection-moulding homopolymers. Processing is normally performed on a reciprocating-screw injection moulding machine equipped with a general-purpose polyolefin screw having an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.0:1 to 3.0:1. Barrel temperatures are commonly maintained from 220 °C to 260 °C, with nozzle temperature between 230 °C and 250 °C. Mould temperature is typically set between 20 °C and 50 °C; the higher end of that range improves surface gloss and reduces flow marks but increases cycle time.
Back pressure is generally set between 5 bar and 10 bar hydraulic pressure, or 0.5 MPa to 1.0 MPa plastic pressure, to homogenise the melt without excessive shear heating. Injection speed is kept medium to high to fill thin-wall cavities before the solidification front closes flow paths. Drying is not required when pellets remain sealed and free of condensation. If surface moisture is present, desiccant drying at 80 °C for 2 h to 4 h is recommended. Melt residence time should be minimised above 260 °C to limit oxidative degradation and the development of yellowing or melt-flow drift.
Mould shrinkage under ISO 294-4 is generally reported in the range of 0.8% to 1.5% along flow and 1.0% to 2.0% across flow depending on wall thickness, packing pressure, and gate geometry. Nucleated solidification narrows the window between the onset of crystallisation and ejection stiffness; cycle-time reductions are therefore possible when the mould cooling design permits uniform heat extraction. Gate freeze-off is influenced more strongly by gate diameter and wall thickness than by melt flow rate alone, and processing data for a specific cavity geometry should be developed rather than inferred from general-purpose moulding guides.
In addition to flow behaviour, the grade exhibits the mechanical response expected of a rigid polypropylene homopolymer. Published datasheet values place tensile stress at yield near 35 MPa under ISO 527-2:2012, with tensile strain at yield of approximately 8%. Flexural modulus under ISO 178:2019 is typically stated near 1550 MPa. Notched Charpy impact strength at 23 °C under ISO 179-1/1eA:2010 is reported at approximately 2.5 kJ/m², reflecting the limited ductility of the homopolymer matrix. Vicat softening temperature under ISO 306 is in the range of 150 °C to 155 °C. These values are representative rather than guaranteed; design calculations should use minimum values from the producer’s specification or confirm property data on production samples.
Thin-wall injection moulding of food containers, disposable cups, caps, closures, and small housewares benefits from the shortened solidification time produced by nucleation. In these applications, part ejection is possible only after the frozen skin acquires sufficient modulus to resist ejection forces. The nucleated morphology of MOPLEN PP HP500N increases nucleation density and reduces spherulite size, allowing a thinner solidified skin to support demoulding. On high-speed packaging cells with hot-runner valve gates, hold time can be reduced when cavity pressure decay is monitored and gate freeze-off is verified; however, published data for a specific hot-runner manifold and cavity geometry may be limited, and production trials should establish the minimum cooling time before cycle-time commitments are made.
Caps and closures produced from this grade are specified for applications requiring stiffness under top load and creep resistance at ambient temperatures. The homopolymer matrix retains a higher modulus at elevated temperature than a random copolymer, but long-term exposure above 80 °C may accelerate relaxation in a pressurised container closure. Closure performance should be evaluated under the relevant torque and sealing standards for the final package, including application torque, removal torque, and leak testing under positive internal pressure.
Regulatory status for food-contact end uses must be confirmed through the producer’s regulatory declaration for the specific finished article. The base polypropylene homopolymer is within the scope of FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011 when all formulation constituents are authorised for the intended food-contact conditions. Overall migration testing under EN 1186 or EU 10/2011 is required on the finished article because migration depends on food simulant, temperature, contact time, and part geometry. The polymer is not intrinsically UV-stabilised; outdoor exposure requires an adequate UV stabiliser masterbatch at dose rates specified by the stabiliser supplier. Avoid prolonged contact with strong oxidising acids, chlorinated solvents, and high-load metal chloride solutions at elevated temperature. The grade is not specifically formulated for medical device or implant use; if such use is contemplated, ISO 10993 biocompatibility evaluation on the final device is required.
| Regulatory reference | Scope | Condition or limitation |
|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymers for food contact | Compliance is formulation-dependent; confirm finished-article status with a producer letter |
| EU Regulation (EU) No 10/2011 | Plastic materials and articles intended for food contact | Overall migration limit of 10 mg/dm² for general food contact; specific migration limits may apply |
| REACH (EC) No 1907/2006 | Registration, evaluation and authorisation of chemicals | Polymer is exempt from registration as a polymer; monomer and additives must be registered |
| RoHS 2011/65/EU | Restriction of hazardous substances in electrical and electronic equipment | Lead, mercury, cadmium, hexavalent chromium, PBB and PBDE below maximum concentration values |
Storage and handling of MOPLEN PP HP500N influence processing consistency. Bags should remain sealed until use, and pellets should be conveyed with low-friction hopper loaders to limit fines generation. If pellet contamination is observed on extended bulk-handling campaigns, dedusting equipment or hopper magnets should be used. The grade is supplied in nominal 25 kg bags or bulk containers according to regional packaging standards. Published data for long-term outdoor storage of this specific grade is limited; indoor storage below 40 °C and away from direct sunlight is recommended to preserve additive performance and colour stability.