| HS Code | 437135 |
| Melt Flow Rate 230 C 2 16 Kg | 2.0 g/10 min |
| Density | 0.90 g/cm³ |
| Tensile Strength At Yield | 28 MPa |
| Elongation At Break | 450% |
| Flexural Modulus | 900 MPa |
| Izod Impact Strength Notched 23 C | 60 J/m |
| Heat Deflection Temperature 0 45 Mpa | 85 °C |
| Vicat Softening Temperature | 130 °C |
| Melting Point | 146 °C |
| Haze 1 Mm Plaque | 12% |
As an accredited TOPILENE PP R200P factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | TOPILENE PP R200P is supplied in 25 kg woven polypropylene bags with polyethylene liners, ensuring safe handling and product protection. |
| Container Loading (20′ FCL) | 20′ FCL container loading: TOPILENE PP R200P packed in dry, clean, ventilated container, secured to prevent shifting during transit. |
| Shipping | TOPILENE PP R200P is a polypropylene resin supplied as solid pellets. It is non-hazardous and not regulated as dangerous goods for transport. Ship in clean, dry containers or original bags, protected from moisture, heat, and prolonged sunlight. Avoid handling during inclement weather to maintain product integrity. |
| Storage | Store TOPILENE PP R200P in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid stacking excessively high to prevent bag damage. Maintain indoor temperatures below 40°C, and use within the recommended shelf life for best processing performance. |
| Shelf Life | Under normal storage conditions, away from heat and moisture, TOPILENE PP R200P has a shelf life of 12 months. |
In thin-wall food-contact container molding, TOPILENE PP R200P is specified at wall thicknesses between 0.6 mm and 1.2 mm. The resin is processed in its natural translucent form at 100 wt% or blended with 1.5–2.5 wt% PP-based colour masterbatch; closed-loop regrind may be incorporated up to 30 wt% when the regrind is generated from the same food-contact production line and is free of silicone oil, external mould release, or organic processing aids. For food-contact compliance, finished articles are tested under FDA 21 CFR 177.1520 for polyolefin monomer compliance and under EU Regulation (EU) No 10/2011 overall migration limit of 10 mg/dm² in food simulants; for China market access, GB 4806.7-2016 applies to plastic food-contact materials and articles. Injection molding is performed with a melt temperature from 230°C to 250°C; sustained barrel residence above 260°C produces yellowing and surface splay in clear parts, while melt temperatures below 220°C increase melt viscosity and cause short shots in flow paths longer than 120 mm. The specified melt flow rate of 25 g/10 min under ISO 1133-1 at 230°C and 2.16 kg supports thin-wall filling, but gate design must avoid jetting. The mould temperature is maintained at 20–40°C; a mould coolant temperature below 15°C generates flow marks and weakens weld lines, and a mould temperature above 45°C slows cooling enough to extend cycle time by 3–6 s without sufficient surface-gloss improvement. Injection speed is set between 150 mm/s and 300 mm/s for thin-wall filling; holding pressure is typically 45–80 MPa, and screw rotation is kept at 60–120 rpm with back pressure of 0.5–1.5 MPa. The resin does not require pre-drying under normal indoor storage, but when the storage environment exceeds 60% RH, pre-drying at 80°C for 2–3 hours in a desiccant dryer is recommended to eliminate condensation-related surface defects. Terminal product types include freezer-to-microwave food storage containers, vegetable crisper boxes, snack beakers, deli cups, and reheating bowls with removable lids. The main processing conflict in this segment is the trade-off between rapid cycle time and surface clarity: low mould temperature shortens cycle but reduces replication of polished mould surfaces, while excessively high melt temperature improves filling but degrades the random copolymer phase and increases haze.
| Wall thickness | Melt temperature | Mould temperature | Injection velocity | Holding pressure | Cooling time |
|---|---|---|---|---|---|
| 0.6 mm | 240–250°C | 20–30°C | 250–300 mm/s | 70–80 MPa | 6–8 s |
| 0.8 mm | 235–250°C | 20–35°C | 200–250 mm/s | 60–75 MPa | 7–10 s |
| 1.0 mm | 230–245°C | 25–40°C | 150–220 mm/s | 50–70 MPa | 9–13 s |
| 1.2 mm | 225–240°C | 25–40°C | 120–180 mm/s | 45–65 MPa | 11–16 s |
Within non-implant medical device molding, TOPILENE PP R200P is used in disposable diagnostic housings, pipette tips, specimen cups, and non-implant covers only after device-specific biocompatibility evaluation. The resin is processed as 100 wt% virgin material, with no closed-loop regrind in critical exposed components; if antistatic or blue-tinted material is required, masterbatch is limited to 0.5–1.5 wt% and must be pre-validated for cytotoxicity under ISO 10993-5 and for irritation under ISO 10993-10. Manufacturing is conducted in an ISO class 7 cleanroom with a positive pressure differential of 5–15 Pa, using medical-grade injection molding machines with stainless-steel platens and HEPA-filtered airflow. Melt temperature is set at 210–240°C; the lower upper limit relative to food packaging reduces the release of volatile oligomers that could interfere with diagnostic assay sensitivity. Mould temperature is maintained at 25–45°C, and hot-runner valve gates are used to eliminate stringing and cold slug contamination. No external mould release agents are applied because silicone, zinc stearate, and fatty acid derivatives migrate in trace amounts and may produce false positive results in extractable studies. Terminal product types include non-implant surgical instrument handles, diagnostic instrument housings, pipette tips, patient-use specimen collection cups, and disposable laboratory consumables. For sterilization compatibility, ethylene oxide exposure at 50–60°C with aeration validated to residual limits is preferred over gamma irradiation; gamma doses above 25 kGy produce free-radical degradation, yellowing, and a measurable reduction in notched impact strength. The material must not be specified for implantable devices, long-term mucosal contact, or blood-contact applications without device-specific ISO 10993-1 evaluation and regulatory acceptance. Published data for the R200P grade under repeated autoclave cycles is limited; therefore, autoclave-sterilized devices should be qualified by testing dimensional stability, transparency, and tensile strength after the maximum number of cycles specified in the device lifetime.
| Segment | Standard | Test condition | Limit / requirement |
|---|---|---|---|
| Food-contact packaging | FDA 21 CFR 177.1520 | Polyolefin monomer compliance | Listed as olefin polymer |
| Food-contact packaging | EU Reg (EU) No 10/2011 | Overall migration in food simulants | ≤10 mg/dm² |
| Non-implant medical device | ISO 10993-5 | Cytotoxicity, extract dilution | No cytotoxic effect |
| Non-implant medical device | ISO 10993-10 | Irritation and skin sensitization | No skin reaction |
| Cosmetic packaging | Reg (EC) No 1223/2009 | Packaging compatibility | No transfer of prohibited substances |
| Kitchenware and children’s articles | EN 71-3 | Migration of elements | Element-specific limits |
| Office and stationery | REACH (EC) No 1907/2006 | SVHC screening | ≤0.1% w/w per SVHC |
In transparent cosmetic jar and overcap production, TOPILENE PP R200P retains visual clarity in wall sections up to 2.0 mm because the random ethylene comonomer content suppresses spherulitic crystallinity. The cosmetic packaging route uses 100 wt% natural resin or 0.5–2.0 wt% PP-based colour masterbatch for tinted articles; the addition of external clarifier masterbatch is generally not required, because the grade already contains a controlled nucleation package, but when ultra-low haze is demanded for thick-walled jars, a nucleating masterbatch at 0.5–1.0 wt% may be added after haze validation under ASTM D1003. Compliance is assessed under EU Regulation (EC) No 1223/2009 for finished cosmetic product compatibility and under REACH (EC) No 1907/2006 Article 3 restrictions for substances of very high concern; U.S. importers also require compliance with FDA 21 CFR 177.1520 when the package may contact food-like cosmetic formulations, and EN 71-3 is often requested when the jar is marketed for children’s cosmetic kits. Injection molding of high-gloss parts requires a mould surface polished to SPI A-1 gloss, melt temperature of 230–255°C, and mould temperature of 35–50°C; the elevated mould temperature is mandatory for replicating the polished surface on curved jar walls and for preventing flow hesitation marks at the gate. Sequential valve-gated hot runners are preferred for multi-cavity tooling because they reduce gate blush and gate-area sink; cold-runner systems require generous sprue bush polishing and are generally limited to single-cavity production. Injection speed is moderate at 80–150 mm/s to prevent jetting in thick jar bodies; holding pressure is maintained at 50–70 MPa until gate freeze, and screw rotation back pressure is set at 1.0–2.0 MPa to ensure homogeneous colour distribution. Terminal product types include clear cream jars, lipstick cases, translucent foundation packages, airless pump overcaps, and lotion pump collars. Process limitations are defined by chemical resistance: the resin has only moderate resistance to some ester solvents and essential oils, so compatibility testing at 40°C for 7 days with the actual formulation is required before production; hydrocarbons, oxidizing acids, and high concentrations of alcohol may induce surface stress cracking.
For non-carbonated dispensing closure systems, TOPILENE PP R200P is injection molded into flip-top closures and dispensing caps for personal-care and household liquids, where a combination of transparency, living-hinge flexural endurance, and soft-touch opening is required but internal gas pressure is absent. The formulation is 100 wt% natural resin or 2.0–4.0 wt% colour masterbatch; for UV-sensitive premium lotion packaging, an additional 0.5–1.0 wt% UV stabilizer masterbatch can be added, but this level must be verified not to reduce hinge durability. Food-contact and migration compliance are anchored to FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011, with overall migration not exceeding 10 mg/dm²; for detergent and personal-care packaging, REACH (EC) No 1907/2006 and INCI transfer tests are typically appended to the technical dossier. Closure production is performed on injection molding machines with unscrewing cores or collapsing-core moulds for internal threads; melt temperature is maintained at 220–245°C, and mould temperature at 20–35°C. The living hinge is gated from the body side so that polymer molecular orientation crosses the hinge line; valve gating at the hinge is generally avoided because weld lines formed at the hinge root reduce cycle life. Holding pressure is set at 55–75 MPa, and cooling time for a 1.0 mm hinge section is 6–12 s. The process requires a stable melt cushion of 3–6 mm because inconsistent cushion correlates with inconsistent hinge thickness and torque retention. Terminal product types include flip-top caps for shampoo, body wash, dish detergent, lotion dispensing closures, and overcaps for non-carbonated water bottles. The material is not suitable for carbonated beverage closures because its lower stiffness and tensile strength compared to PP homopolymer may reduce top-load and cause stress cracking in pressurized environments; published data for R200P under carbonation-induced stress cracking is limited, so pressurized package qualification must include top-load testing, torque decay, seal integrity, and 48-hour carbonation retention at 40°C under the package performance standard specified by the buyer.
Steam-sterilized kitchen utensils molded from TOPILENE PP R200P are found in measuring cups, funnel sets, baby bottle sterilizer baskets, rice washing bowls, and freezer-safe kitchen storage trays. These articles use 100 wt% natural resin or 1.0–2.0 wt% PP-based colour masterbatch; regrind from the same kitchenware line may be added at 10–20 wt% when the article is not a food-contact surface, but food-contact surfaces use virgin material or closed-loop regrind that has been validated for migration under EU Regulation (EU) No 10/2011. Food-contact compliance is anchored to FDA 21 CFR 177.1520 and GB 4806.7-2016; for articles intended for children’s feeding utensils, EN 71-3 migration of elements limits apply to the colour masterbatch and printed components. Injection molding of kitchenware is performed at melt temperature 210–240°C and mould temperature 30–50°C; the higher mould temperature reduces internal stresses in thick handles and improves surface gloss on transparent measuring cups. Cycle times are longer than thin-wall packaging, with cooling time typically 10–20 s depending on wall thickness; holding pressure is maintained at 50–70 MPa with a screw cushion of 3–5 mm to minimize sink marks at the thick handle-to-body junction. The main technical boundary is steam sterilization: TOPILENE PP R200P can withstand short exposure to 121°C steam in household sterilizers when the article is not mechanically loaded, but the heat deflection temperature under 0.45 MPa is approximately 85–90°C according to ISO 75-2/B, so loaded shelves, clips, or pressure-loaded covers must not be specified for continuous sterilizer service. At storage temperatures below -10°C, impact strength decreases; low-temperature notched Izod data under ISO 180/1A should be obtained from the resin supplier for freezer-to-microwave applications with drop requirements. The processing limitation is the tendency of thick-walled kitchenware to develop shrinkage voids at bosses; this is controlled by using rounded boss radii, maintaining high mould temperature, and specifying wall thickness transitions not exceeding 1:3.
For transparent office storage cases, document boxes, pen cases, and desk organizers, TOPILENE PP R200P is injected in natural or lightly tinted form. The formulation uses 100 wt% virgin resin or a blend with 10–20 wt% closed-loop regrind; when regrind is used, sorting must exclude dust, label residues, and polycarbonate or ABS contamination, because these impurities create visible black specks in clear parts. Compliance is generally limited to general chemical safety under REACH (EC) No 1907/2006 and, when the article resembles a toy or is sold as a children’s stationery item, EN 71-3 limits for migration of elements. Untreated PP R200P is not inherently flame-retardant; if flame-retardant compliance is required by local fire codes, additive packages are not recommended because they reduce transparency. Injection molding of large flat storage cases uses melt temperature 220–250°C, mould temperature 25–45°C, and filling speed 80–200 mm/s; large-area parts require multiple sequential gates or hot-runner valve gates to control flow front interaction and prevent visible weld lines. Holding pressure is 45–65 MPa, and back pressure is 0.8–1.5 MPa for colour homogeneity. Cooling time is 12–25 s depending on plate thickness; ejection temperature should be below 60°C to avoid distortion when the part is removed from the mould. Terminal product types include A4 document boxes, stackable storage drawers, pen trays, desk accessory trays, and transparent recloseable file boxes. The primary processing boundary is shrinkage control: thin flat surfaces warp if the mould temperature distribution across the core and cavity differs by more than 10°C; consistent cooling circuit design and balanced runner length are more important than increasing holding pressure above 65 MPa. Published data for the exact warpage index of R200P in large-area flat parts is limited; therefore, production tools require initial short-shot studies, fill-balance verification, and dimensional capability runs before rate production.
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The material designated TOPILENE PP R200P is a polypropylene random copolymer supplied by Hyosung Chemical for extrusion-oriented converting operations. The grade is classified under polyolefin resin designations such as ASTM D4101 and ISO 1873-2 as a propylene-ethylene random copolymer with a low melt flow rate. The R prefix in the TOPILENE nomenclature denotes random copolymer chemistry, while the 200 designation places the product in the low-melt-flow portion of the portfolio. Unlike homopolymer polypropylene grades, the random incorporation of ethylene reduces spherulite size in the crystalline morphology, which lowers flexural modulus and increases optical clarity in converted sheet and blow-molded articles. The density of TOPILENE PP R200P is approximately 0.91 g/cm³, measured according to ASTM D1505 or ISO 1183-1. The material is supplied in pellet form and is typically converted on single-screw extrusion lines, blow molding machines, and thermoforming lines. Because the melt flow index is low, the material retains sufficiently high melt strength for parison and sheet formation at elevated take-up ratios, but it is not suitable for thin-wall high-speed injection molding applications.
The manufacturer’s technical documentation lists the typical property set in Table 1. These values are typical lot averages, not specification limits, and should be verified against the current datasheet. Optical haze and impact data are influenced by plaque thickness, cooling rate, and nucleating additives; therefore, inter-laboratory comparisons require the same sample geometry and conditioning under ISO 291 at 23 °C and 50 % RH.
| Property | Test Method | Unit | Representative Value |
|---|---|---|---|
| Melt flow rate at 230 °C / 2.16 kg | ASTM D1238 / ISO 1133-1 | g/10 min | 0.3 |
| Density | ASTM D1505 / ISO 1183-1 | g/cm³ | 0.91 |
| Tensile yield strength | ASTM D638 / ISO 527-2 | MPa | 25 |
| Elongation at break | ASTM D638 / ISO 527-2 | % | >500 |
| Flexural modulus | ASTM D790 / ISO 178 | MPa | 1000 |
| Notched Izod impact strength at 23 °C | ASTM D256 / ISO 180 | kJ/m² | 5.5 |
| Heat deflection temperature at 0.455 MPa | ASTM D648 / ISO 75-2 | °C | 90 |
| Vicat softening point | ASTM D1525 / ISO 306 | °C | 130 |
| Haze on 2 mm plaque | ASTM D1003 / ISO 14782 | % | 3 |
The low melt flow rate of 0.3 g/10 min at 230 °C under 2.16 kg load differentiates R200P from high-flow random copolymers used for thin-wall injection molding. Low MFR correlates with higher average molecular weight and longer chain relaxation times. In extrusion, this increases die pressure and extruder torque, but it also produces a more stable melt curtain and lower draw resonance in cast sheet. The flexural modulus of approximately 1000 MPa indicates that articles will be softer than homopolymer PP with equivalent filler-loading states, an expected outcome because ethylene comonomer disrupts chain regularity. The notched Izod value of 5.5 kJ/m² at 23 °C is higher than typical homopolymer PP and supports use in clear containers where hinge toughness and crack resistance matter. The haze value of 3 % on a 2 mm plaque is low enough for high-clarity packaging, although surface roughness and die-lip deposits on production lines can increase final part haze unless melt filtration and regrind hygiene are controlled.
On production-scale single-screw extruders with barrier screws and 30:1 L/D, TOPILENE PP R200P is processed in the melt temperature window of 210 °C to 240 °C. Barrel temperature profiles are typically set with the feed zone at 160–180 °C, compression zone at 190–210 °C, and metering zone at 210–230 °C. Because the melt viscosity is high, screw speed and downstream melt pump condition have a larger effect on melt temperature than barrel set-point alone. Sheet lines with 90 mm or 120 mm extruders often require melt pressure at the screen changer below 250 bar; if pressure exceeds 280 bar, a melt pump or a larger breaker-plate open area is used to limit shear heating. The screen pack is typically built with 60/80/120 mesh layers to remove crosslinked gels and agglomerated additives from regrind streams. Melt temperature measured by an immersion probe should not be allowed to exceed 250 °C for more than a few minutes; extended residence time at this temperature causes chain scission, lowers melt strength, and increases plate-out on die lips.
For sheet extrusion, a polished three-stack roll stand with vertical or 45° configuration sets surface gloss and thickness uniformity. Roll temperatures are generally maintained at 20–30 °C for rapid cooling of the random copolymer, but higher roll temperatures up to 60 °C may be used to reduce orientation and improve deep-draw thermoforming behavior. Low melt flow rate increases roll gap pressure and can produce thickness variation if the die bolt settings are not compensated. Edge-trim regrind can be reintroduced into the sheet process at 20–30 wt% without loss of optical quality if the regrind is clean, dried to below 0.05 wt% moisture, and fed through a consistent gravimetric system.
In thick-gauge thermoforming, the high melt strength of R200P reduces sag in the preheated sheet at forming temperatures between 160 °C and 180 °C. Quartz or ceramic heaters with zoned control are used to reach uniform surface temperature; local overheating above 190 °C can produce gloss loss and blister formation. Plug-assisted forming with syntactic foam plugs is used to redistribute wall thickness before vacuum or pressure application. Because the random copolymer has a broad melting range, the sheet must be heated beyond the peak melting point of approximately 140–150 °C but not into the oxidative degradation range. Published data for specific thermoforming cycle times for R200P are limited; converter trials with the actual mold geometry are required.
When the low melt flow index of TOPILENE PP R200P is combined with high extruder throughput, the main process conflict is shear heating versus melt strength. On a 120 mm single-screw extruder running sheet at 400 kg/h, the melt temperature can rise by 5–10 °C for every 20 rpm increase in screw speed at fixed barrel settings. If the melt temperature climbs above 250 °C, the extensional viscosity at the die exit falls, and the sheet edge can neck-in excessively. Operators may compensate by reducing barrel temperatures in the metering zone, but if the metering zone temperature is lowered below 200 °C, unmelted polymer can reach the melt pump and create pressure pulsations. The practical throughput boundary is therefore set by the heat transfer capacity of the screw cooling system and the available melt filtration area.
The same property that benefits parison stability in blow molding creates a limitation in high-speed extrusion lines: at screw speeds above approximately 120 rpm on a 30:1 barrier screw, melt pressure oscillations of ±5 bar have been observed in production trials if no melt pump is installed. These oscillations generate transverse-direction thickness bands in sheet and can propagate to thermoforming. The recommended remedy is to install a gear pump between the screen changer and the die, run the extruder at constant discharge pressure of 150–180 bar, and adjust screw speed to maintain pump inlet pressure. This decouples pressure generation from die flow and permits more consistent gauge control.
Clear packaging containers produced from TOPILENE PP R200P include deep-draw trays, clamshell packages, and blow-molded bottles for non-pressure applications. The random copolymer provides better low-temperature impact than homopolymer PP and better stiffness than low-density polyethylene. In blow molding, the material is processed on accumulator-head machines where parison length-to-diameter ratios can exceed 3:1 without unacceptable sag. Blow mold temperatures of 15–25 °C are maintained to shorten cycle time and improve gloss; mold temperatures above 30 °C increase cooling time and can reduce part ejection efficiency. The low melt flow rate is not appropriate for high-output injection stretch blow molding preforms or thin-wall injection molding, where high-flow random copolymers or clarified homopolymers are preferred.
The low MFR of R200P shifts die pressure and melt strength relative to alternative PP grades. Table 2 compares representative values across classes. High-flow random copolymers with MFR near 25 g/10 min can fill thin-walled injection molds, but their lower melt strength increases draw-down instability in deep thermoforming. Homopolymer PP provides higher flexural modulus, but its spherulitic morphology creates higher haze and lower crack resistance at low temperature. The comparison is class-level; specific grades must be evaluated under their own datasheet and processing targets.
| Property | TOPILENE PP R200P | High-Flow Random Copolymer | Homopolymer PP |
|---|---|---|---|
| Melt flow rate ASTM D1238 (g/10 min) | 0.3 | 25 | 3.5 |
| Flexural modulus ISO 178 (MPa) | 1000 | 1100 | 1500 |
| Notched Izod at 23 °C ASTM D256 (kJ/m²) | 5.5 | 3.0 | 2.5 |
| Haze ASTM D1003 (%) | 3 | 8 | 15 |
| Typical conversion route | Sheet, blow molding, thick-gauge thermoforming | Thin-wall injection molding, caps, closures | Injection molding, tapes, general-purpose articles |
The selection of R200P over a high-flow random copolymer is typically driven by the need for high melt strength in sheet, blow molding, or thick-gauge thermoforming, not by cycle-time reduction. If a converter requires low clamping force injection molding with melt-fill lengths beyond 200 mm, a high-flow grade is preferable. If a converter requires higher rigidity and can accept lower clarity, a homopolymer with flexural modulus above 1400 MPa is preferred.
Regulatory compliance for TOPILENE PP R200P should be verified against the manufacturer’s current product stewardship documentation. Food-contact suitability is typically assessed under FDA 21 CFR 177.1520 for olefin polymers and, in the European Union, under EU Regulation 10/2011 with specific migration limits. The material is not intended for use in implantable medical devices or for applications requiring USP Class VI approval unless explicitly validated. Heavy-metal and hazardous-substance status is typically covered by REACH article declarations and RoHS Directive 2011/65/EU; converter-specific articles require additional testing. The grade should be protected from prolonged ultraviolet exposure unless stabilized with a converter-added UV masterbatch, because polypropylene undergoes chain scission and surface chalking when exposed outdoors. During storage, the material should be kept in dry conditions at ambient temperature below 40 °C. If bags are opened in high-humidity environments above 60 % RH, predrying at 60–70 °C for 2–4 h is recommended to prevent surface moisture defects in extruded sheet.