| HS Code | 906076 |
| Density | 0.90 g/cm³ |
| Melt Flow Rate 230 C 2 16 Kg | 12 g/10 min |
| Tensile Stress At Yield | 25 MPa |
| Elongation At Yield | 10% |
| Flexural Modulus | 900 MPa |
| Izod Impact Strength Notched 23 C | 5 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 70°C |
| Vicat Softening Point 10 N | 120°C |
| Rockwell Hardness | R85 |
| Haze | 12% |
As an accredited Jampilen PP Terpolymer RP127K factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg multi-wall paper bags, with palletized and stretch-wrapped units for safe transport. |
| Container Loading (20′ FCL) | Load 20′ FCL with Jampilen PP Terpolymer RP127K in palletized woven PP bags, shrink-wrapped, evenly distributed for safe transport. |
| Shipping | Jampilen PP Terpolymer RP127K ships as non-hazardous plastic pellets in sealed moisture-resistant bags or bulk containers. Keep dry, avoid excessive heat and direct sunlight, store in ventilated area. Handle with clean equipment to prevent contamination. No special transport restrictions apply under standard conditions. |
| Storage | Store Jampilen PP Terpolymer RP127K in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep original containers tightly sealed to prevent moisture pickup and contamination. Avoid generating dust; use proper grounding to prevent static accumulation. Maintain warehouse temperatures below 40°C and protect from mechanical damage. |
| Shelf Life | Shelf life is typically two years from manufacture when stored in a cool, dry, shaded area with original packaging intact. |
Jampilen PP Terpolymer RP127K is converted primarily as a low-seal-initiation skin layer in three-layer and five-layer cast polypropylene film lines. Published data for this specific grade remain limited in independent technical literature; the processing windows below derive from propylene-ethylene-butene terpolymer class behaviour and require confirmation against producer data obtained under ISO 1133-1 and ISO 1183-1. In cast film coextrusion, the sealant skin is maintained at 3–7 µm to provide seal initiation without excessive blocking. The core layer is typically a homopolymer or block copolymer for stiffness. Melt temperature at the flat die is set from 220 °C to 240 °C. Die gap is held between 0.4 mm and 0.8 mm. The chill roll surface is controlled at 20–28 °C. Heat sealability is measured according to ASTM F2029. Seal strength after lamination is tested under ASTM F88/F88M. Optical haze is measured by ASTM D1003. Coefficient of friction is determined by ASTM D1894.
Anti-block addition to the sealant skin is usually specified at 0.1–0.3 wt% synthetic amorphous silica with a median particle size of 2–6 µm. The formulation is a compromise. Loadings above 0.3 wt% can raise haze above 8% in a 25 µm film and reduce seal strength by creating surface defects. Loadings below 0.05 wt% may allow blocking on the rewinder. The failure appears as stick-slip noise and fine circular pick-off marks on the printed film surface. On production-scale cast lines, blocking is quantified by measuring peel force between adjacent wound wraps. The low crystalline fraction of the terpolymer increases migration speed of primary amide slip additives. The coefficient of friction can fall below target within 24 h to 48 h after winding instead of the 72 h seen with homopolymer sealant skins. Slip agent migration kinetics should be validated under ASTM D1894 after storage at 40 °C.
Food-contact compliance is governed by 21 CFR 177.1520(c) for olefin polymers in the United States and by EU 10/2011, Annex I, Table 1 for authorised monomers in the European Union. Overall migration is limited to 10 mg/dm² under EU 10/2011, Article 12. The end articles include printed laminates for snack foods, confectionery, dry cereal pouches, and other dry or fatty food packaging where a peelable or destruct seal is required.
When a terpolymer skin is coextruded onto a BOPP base web and oriented sequentially, the final skin thickness after transverse stretching is typically 0.5–1.0 µm. Machine-direction stretching is performed at 4.5:1–5.5:1 with roll temperatures between 120 °C and 135 °C. Transverse stretching follows at 8:1–10:1 in a tenter oven with preheat zones at 150–165 °C. The terpolymer layer must not stick to the MDO rolls. Anti-block particle size and surface roughness therefore become dominant control variables. Film splits in the tenter occur if the edge bead thickness before orientation exceeds 8 µm, because the low-melting skin cools below the draw temperature at the edge.
Seal initiation is recorded under ASTM F2029, but hot tack under ASTM F1921 has a finite plateau. At seal bar temperatures above approximately 140 °C, the sealant layer loses cohesive integrity before the bond cools and the hot tack force drops sharply. The operating window on a vertical form-fill-seal line is therefore controlled by jaw dwell time between 0.2 s and 0.6 s and by seal bar pressure below 0.4 MPa. Line speeds of 40–80 packages/min are achievable when the seal initiation temperature remains 10–15 K below that of a random ethylene-propylene copolymer. Published hot-tack curves for this specific RP127K configuration are limited. Each film structure should be validated on the target machine with filled packages and jaw temperature profiling.
Blown film conversion of a low-melting polypropylene terpolymer requires a high-melt-strength core layer. Bubble instability appears at blow-up ratios above 2.0:1 when the skin layer has no crystallinity support. The die gap is set between 0.8 mm and 1.2 mm, melt temperature is held at 200–220 °C, and dual-lip air-ring cooling keeps the frost line below 150 mm. The sealant layer thickness after extrusion is 8–15 µm in a total film of 40–70 µm. Frozen vegetables, pastry bags, and ice cream pouches are sealed at 115–125 °C and then distributed at −25 °C. Seal integrity after frozen storage is checked on filled pouches by drop testing according to ASTM D5276 and by peel testing according to ASTM F88/F88M.
Ethylene oxide-sterilised flexible pouches for medical devices impose a minimum seal strength of 1.5 N/15 mm under EN 868-5:2018, Annex D. The terpolymer film is used as a transparent lidding web on a polyolefin-coated tray or as the polymeric side of a paper/plastic pouch. Sealant layer thickness is typically 20–40 µm in solvent-free laminations. Sealing temperature is kept below 130 °C to avoid tray distortion. Sterilisation validation follows ISO 11135:2014 for ethylene oxide. Package integrity is tested by ASTM F1929 for porous packaging dye penetration. Cytotoxicity is evaluated according to ISO 10993-5 where the film contacts body tissue or fluid-path devices. Tear propagation in the seal area is monitored by ASTM D1938; a mode transition from cohesive peeling to adhesive delamination is interpreted as contamination or excessive seal dwell.
| Regulatory or Test Reference | Application Scope | Key Clause or Method |
|---|---|---|
| 21 CFR 177.1520 | Olefin polymers for food contact | Extraction limits in §177.1520(c) |
| EU 10/2011 | Food-contact plastics | Annex I Table 1; OML 10 mg/dm² under Article 12 |
| GB 4806.7-2016 | Plastic food-contact materials in China | Overall migration and consumption limits |
| EN 868-5:2018 | Paper/plastic pouches for terminally sterilised devices | Minimum seal strength 1.5 N/15 mm, Annex D |
| ASTM F2029 / F88/F88M / F1921 | Heat sealing, seal strength, hot tack | Seal initiation, peak force, hot tack plateau |
Extrusion coating of a terpolymer sealant onto aluminium foil is conducted at 260–290 °C. A thin tie layer of maleic anhydride-grafted polypropylene is required to prevent interlayer delamination. The cooling roll is maintained at 15–20 °C and the coat weight is held at 10–15 g/m². The structure eliminates a solvent-based adhesive lamination stage and is used for chocolate and sugar confectionery wrappers. The process window is narrow because the low-melting fraction oxidises to gel particles at melt temperatures above 300 °C during extended continuous runs. Gel severity is evaluated by counting visible defects per square metre on the coated foil under reflected light. No published data are available for this exact RP127K extrusion-coating configuration. A trial on a pilot coater with a 30:1 L/D screw and 0.7 mm slot die is considered necessary before production commitment.
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Jampilen PP Terpolymer RP127K is a propylene-based terpolymer resin positioned for coextruded cast film, blown film, and heat-seal layers in flexible packaging. The grade is specified where a lower seal initiation temperature is required than that of conventional propylene random copolymers, without moving to all-olefin elastomer sealing layers. In a multilayer structure, RP127K reduces the temperature at which the sealant layer forms a hermetic bond while retaining polyolefin-based clarity, low moisture transmission, and acceptable packaging-line handling. The product differs from homopolymer polypropylene and standard random copolymer grades mainly by the presence of an additional comonomer beyond ethylene, which reduces crystalline order and broadens the melting range. Because the exact comonomer ratio is not always disclosed in public summaries, the manufacturer certificate of analysis and lot-specific data should be consulted for target melt flow rate, flexural modulus, and seal initiation temperature. Published data for this specific configuration is limited in some public sources; therefore, process decisions should be benchmarked against ISO and ASTM methods applied to the actual lot.
Seal initiation temperature in a terpolymer film is governed by compositional heterogeneity in the crystalline phase rather than by a single melting point. DSC measurements conducted per ISO 11357-3 on propylene-ethylene-butene terpolymers generally show a broad melting range; the lower end of that distribution determines the temperature at which surface crystals become sufficiently mobile to interdiffuse under jaw pressure. Seal initiation, often measured by a heat-seal tester according to ASTM F1921-12(2023) or seal strength by ASTM F88/F88M-21, commonly falls below 100 °C for the terpolymer class when film thickness is in the 20 µm to 50 µm range. The additional comonomer shortens the average methylene sequence length, reduces the equilibrium melting temperature, and broadens the distribution of lamellar thicknesses. That broadening is useful for seal performance but imposes constraints: the same molecular feature lowers Vicat softening temperature and limits sustained-use temperature, as measured by ISO 306 or ASTM D1525-17e1. A lower seal initiation temperature cannot be optimized independently of stiffness and heat deflection; increasing comonomer content to gain a few degrees of seal advantage can reduce tensile yield stress below the value required for high-speed packaging lines.
Additive packages containing slip agents, anti-block agents, or nucleators also alter seal response. Nucleating agents may raise crystallization temperature and narrow the melting distribution, which can increase haze but also sharpen the onset of seal initiation. Migration of slip aids to the seal surface can reduce coefficient of friction but, if dosed incorrectly, may depress seal strength. The reported lower seal initiation should therefore be confirmed on the final film structure, not on resin pellets alone.
Incoming resin verification for RP127K should include a defined test matrix. The manufacturer certificate of analysis normally reports melt mass-flow rate, density, tensile yield stress, flexural modulus, notched impact strength, and thermal parameters. The following methods are relevant; values should be compared against the producer specification band rather than generic literature values.
| Property | Test method | Role in lot acceptance |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 at 230 °C/2.16 kg | verifies extrusion viscosity level |
| Density | ISO 1183-1 | confirms composition class and crystalline fraction |
| Tensile yield stress and elongation | ISO 527-2 | indicates stiffness and film strength |
| Flexural modulus | ISO 178 | indicates sealant stiffness in laminate |
| Notched Charpy impact | ISO 179-1 | indicates low-temperature film toughness |
| Vicat softening temperature | ISO 306 | operational temperature limit |
| Melting and crystallization | ISO 11357-3 | seal temperature and thermal processing window |
| Haze | ASTM D1003-21 | optical clarity of film |
| Gloss at 60° | ASTM D2457-21 | surface appearance |
| Coefficient of friction | ISO 8295 | packaging line runnability |
| Seal initiation | ASTM F1921-12(2023) | final seal performance |
| Food-contact migration | EU 10/2011, FDA 21 CFR 177.1520 | compliance for sensitive packaging |
A lot should be considered acceptable only if the measured MFR is within producer tolerance. Melt flow rate should not be evaluated in isolation because comonomer variations can shift MFR even when final film properties remain acceptable. When incoming resin is stored at relative humidity above 60%, surface moisture may produce bubbles in cast film; pre-drying at 80 °C for 2 h to 4 h in a dehumidified-air hopper dryer is often sufficient. Drying above 100 °C for extended periods is to be avoided because oxidative yellowing can occur in unstabilised grades. The exact drying recommendation should be checked against the producer safety data sheet.
On a production-scale cast-film line with a single-screw extruder of 45 mm to 90 mm diameter and L/D ratio of 30:1 to 33:1, a propylene terpolymer of moderate melt flow rate is typically processed at a melt temperature of 220 °C to 250 °C. Barrel profiles commonly start at 180 °C near the feed throat and rise to 240 °C at the die adapter. The screw should incorporate a barrier section and a distributive mixing element; without these, comonomer-rich domains can produce streak defects in thick cast film and inconsistent seal performance. If melt temperature exceeds 270 °C, chain scission accelerates, yellowness index may increase, and seal strength may decline due to the formation of low-molecular-weight oxidized species.
Chill-roll temperature is a critical process variable. Chill-roll temperatures between 15 °C and 25 °C produce the low haze required for clear sealant webs, but temperatures below the plant dew point can condense moisture on the roll, causing surface defects. When chill rolls operate below 10 °C, condensation control through dehumidification is required. Conversely, increasing chill-roll temperature above 35 °C slows crystallization and can produce a hazy film with poor dimensional stability. The process window is therefore narrower for terpolymer sealant layers than for many random copolymers because the lower crystalline order shifts the optical and morphology balance.
Edge-trim reclaim can be re-pelletized and blended into the sealant layer, but the blend ratio should be kept below 30% unless the film line is equipped with gravimetric dosing and on-line haze measurement. Higher reclaim addition can increase gel counts because the sealant layer sees repeated heat history at the die lip and in the regrind step. Batch-to-batch variance in comonomer content should be monitored by comparing the DSC melting trace of the incoming lot with a reference lot; a shift of more than 3 °C in the main melting peak may require seal-bar temperature adjustment. These production-scale checks are necessary because lot-specific comonomer distribution can change the thermal and rheological response even when the MFR remains within specification.
Optical and mechanical performance of cast film based on RP127K should be assessed after extrusion, not on resin pellets. Haze per ASTM D1003-21 in a 25 µm cast film generally falls below 5% for clean, well-chilled terpolymer sealant layers; gloss at 60° per ASTM D2457-21 is usually above 80 GU. These values are representative for the propylene terpolymer class and may vary with chill-roll polish, die lip cleanliness, and additive package. Dart impact strength per ISO 7765-1 or ASTM D1709 is influenced by film thickness and coextruded tie-layer adhesion; in asymmetric multilayer structures, failure often initiates at the sealant layer because lower modulus reduces puncture energy. Therefore, comparison with homopolymer or random copolymer films should be made at equal film thickness and layer ratio.
Food-contact status should be verified against the final film formulation and layer migration results. Polypropylene homopolymer and copolymer grades used in food contact are generally assessed under FDA 21 CFR 177.1520 and EU Regulation 10/2011; the specific grade must meet the applicable overall migration limit and substance-specific restrictions. The processor is responsible for confirming that cleaning solvents, printing inks, and lamination adhesives do not interact with the sealant layer. Incompatible additives include certain amine-based antistatic agents and acidic species that can accelerate ageing or produce organoleptic failures in sensitive packaging applications. Storage under direct UV or in humid environments without sealed packaging should be avoided. The producer safety data sheet should be consulted for REACH registration status and candidate-list substances; RoHS Directive 2011/65/EU restricts lead, cadmium, mercury, hexavalent chromium, PBB, and PBDE, although unmodified polypropylene resin typically falls below the maximum concentration values in homogeneous material.
Substitution of a random copolymer sealant with RP127K requires more than a simple pellet change. The lower seal initiation temperature may permit a reduction in seal-bar setpoint of 10 °C to 20 °C, but the same material also has lower modulus and higher elongation at break. This changes the stress distribution in the film; on high-speed vertical form-fill-seal machines, the sealant layer may stretch differently during film transport. Machine-direction tensile modulus measured by ISO 527-3 on the final film should be evaluated before reducing film thickness. Because terpolymer sealant layers are often softer, downstream packaging machinery may require adjustment of dancer tension or sealing jaw dwell time.
Compared with a propylene homopolymer, RP127K has a substantially lower heat deflection temperature and is not suitable for hot-fill, retort, or microwave-only structures requiring high thermal stability. Compared with a standard random copolymer, the terpolymer provides lower seal initiation and often superior clarity, but the difference in stiffness becomes measurable in flexural modulus and in the force required to dispense film from a roll. The selection should therefore be based on the seal-temperature requirement of the packaging line and the thermal resistance of the substrate. In coextrusions where the sealant layer is less than 10% of total thickness, the overall film stiffness remains controlled by the core layer; in such cases, the penalization from terpolymer softness is minimal. In thicker monolayer or sealant-dominant structures, the stiffness reduction is more apparent and should be compensated by layer-ratio adjustment or by selecting a lower-comonomer terpolymer grade if the seal-temperature benefit is still sufficient.