| HS Code | 607655 |
| Melt Flow Rate 230 C 2 16 Kg | 8 g/10min |
| Density | 0.9 g/cm³ |
| Tensile Strength At Yield | 27 MPa |
| Elongation At Yield | 12% |
| Flexural Modulus | 1100 MPa |
| Izod Impact Strength Notched 23 C | 5 kJ/m² |
| Vicat Softening Temperature | 130 °C |
| Heat Deflection Temperature 0 45 Mpa | 85 °C |
| Melting Temperature | 146 °C |
| Rockwell Hardness | R 85 |
As an accredited Jampilen PP Terpolymer RP129K factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Jampilen PP Terpolymer RP129K is supplied in 25 kg polyethylene-lined paper bags, palletized and stretch-wrapped for safe transport. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Jampilen PP Terpolymer RP129K ensures secure, dry stowage of palletized bags, preventing moisture and damage during transit. |
| Shipping | Jampilen PP Terpolymer RP129K is a non-hazardous polypropylene terpolymer supplied as free-flowing pellets. It is not regulated as dangerous goods for transport. Pack in clean, dry 25 kg bags or bulk containers. Keep away from excessive heat, ignition sources, and moisture during transit. |
| Storage | Store Jampilen PP Terpolymer RP129K 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. Maintain ambient temperatures and good housekeeping to minimize fire risks and preserve material quality. |
| Shelf Life | Store in a cool, dry place away from UV light. Typical shelf life is 12 months from delivery date. |
On three-layer and five-layer cast polypropylene lines equipped with barrier screws of 30:1–35:1 L/D and screw diameters of 75–120 mm, RP129K is assigned to the sealing skin at a thickness of 8–20 µm. The extruder barrel profile for the terpolymer skin is normally set between 220 °C rear zone and 245 °C die zone, with the melt discharged through a T-slot die having a die gap of 0.5–0.8 mm. A dual-chamber vacuum box and air knife fix the melt curtain onto a polished chill roll maintained at 18–24 °C. The propylene-ethylene-butene structure reduces crystalline order compared with an ethylene-propylene random copolymer; on a 50 µm three-layer cast film, haze below 2.0% under ASTM D1003 and 45° gloss above 85 GU under ASTM D2457 are achievable when the chill roll surface roughness is below 0.5 µm Ra. Heat seal initiation under ASTM F2029 with 40 psi jaw pressure and 0.5 s dwell typically shifts to 105–115 °C for a 15 µm skin. Seal strength measured per ASTM F88/F88M on 25 mm strips reaches a plateau of 8–12 N/25 mm when the jaw temperature is 120–140 °C. The sealing plateau may extend 15–20 °C before the film shrinks or adheres to the jaw, which is the primary advantage of the broader crystallite size distribution. On production lines running above 80 m/min, a skin gauge below 5 µm exhibits longitudinal thickness variation that causes intermittent seal voids. The failure mechanism is not mechanical weakness but the interaction of melt draw resonance, edge bead pinning, and the wider melting range of the terpolymer. Slip and antiblock masterbatch addition should not exceed 2–4 wt% for silica-based antiblock with a particle size d50 of 3–5 µm and erucamide slip at 800–1,200 ppm. Higher loading raises seal initiation by 3–6 °C and reduces interlayer adhesion. After seasoning, kinetic COF of the sealant surface is normally 0.20–0.30 under ASTM D1894; a value above 0.40 causes drag in form-fill-seal tracks. For food-contact use, the finished cast film must comply with US FDA 21 CFR §177.1520 and EU Regulation (EU) No 10/2011; overall migration testing is performed on the final laminated or coated structure, not on the neat resin.
On rotary vertical form-fill-seal equipment with jaw dwell times of 0.25–0.50 s and capacities of 80–120 bags/min, the sealant layer in a three-layer PE/PP film must develop hot-tack force above 1.5 N/25 mm immediately after jaw release. RP129K is incorporated as the inner sealant layer at 8–15 µm, coextruded with a metallocene LLDPE or MDPE core to prevent blocking. Hot-tack measurements per ASTM F1921/F1921M at a seal pressure of 0.3 MPa and a cool time of 0.1–0.2 s show that the terpolymer retains molten-phase tack over a wider jaw-temperature interval than an ethylene-propylene random copolymer of equivalent MFR. The practical plateau is 115–135 °C, but it narrows when the RP129K layer is diluted with more than 30 wt% propylene homopolymer because homopolymer crystallites freeze at the seal interface before molecular diffusion across the weld is complete. In a heat-seal tester set at 0.3 s dwell and 0.4 N/mm² pressure, a drop in hot-tack strength below 1.0 N/25 mm correlates with package burst failures after filling hot liquid at 85 °C. The failure mode is typically interfacial seal peel rather than film tear, visible as a glossy separation surface. Rotary jaw misalignment greater than 0.05 mm across the seal bar length produces local cold spots that cannot be corrected by raising jaw temperature above 140 °C without introducing edge shrinkage. The line team must monitor seal bar temperature variation with a contact thermocouple and maintain the differential across the bar within ±3 °C. A jaw release angle of 4–6° and a stripper plate temperature below 60 °C are necessary to prevent stringing, which is more pronounced in terpolymer skins than in homopolymer skins because the molten seal can extend over a broader temperature range.
| Sealant layer configuration | Seal initiation range under ASTM F2029 | Peak hot-tack range | Observed VFFS failure mode |
|---|---|---|---|
| 100 wt% RP129K, 15 µm | 105–115 °C | 1.8–2.5 N/25 mm at 125 °C | No burst up to 100 cycles/min |
| 80/20 wt% RP129K/homopolymer PP, 15 µm | 112–122 °C | 1.2–1.8 N/25 mm at 130 °C | Occasional peel at >80 cycles/min |
| 15 µm RP129K with 3 wt% high-slip masterbatch | 109–119 °C | 1.5–2.0 N/25 mm at 125 °C | Slight stringing at >90 cycles/min |
In collation shrink film, RP129K is used at 10–20 wt% in the outer layers of a 50–80 µm three-layer or five-layer blown film to lower the orientation temperature and improve transverse direction shrink at 90–110 °C without sacrificing bubble stability. The bubble is quenched at a frost-line height of 600–900 mm from the die, with a blow-up ratio of 4.0:1–5.5:1 and a lay-flat width variation held within ±5 mm. Shrinkage measured per ASTM D2732 in a silicone oil bath at 100 °C for 30 s is typically 55–65% in transverse direction and 5–10% in machine direction for 60 µm film. The low crystalline melting point of the terpolymer reduces the tunnel set point needed to complete transverse shrinkage: a steam tunnel at 85–95 °C or a hot-air tunnel at 95–105 °C provides full package conformance. If the tunnel temperature is pushed beyond 115 °C, the terpolymer-rich outer surface develops micro-adhesion to conveyor belts and causes labeling defects. The primary processing conflict is between low-temperature shrink force and ambient storage stability. At warehouse temperatures above 35 °C, partially oriented terpolymer film can exhibit premature shrink of 2–4% in transverse direction. This is managed by annealing rolls after orientation at 40–50 °C for 30–60 s and by controlling the terpolymer addition level. A higher butene comonomer content in RP129K lowers the crystalline melting range, so the incoming resin lot should be characterized by differential scanning calorimetry under ISO 11357-3; the ratio of lower to higher melting shoulders shifts the shrink-initiation temperature by several degrees. Published lot-specific data for RP129K in this exact collation-shrink configuration may be limited, so the residual shrink after annealing should be verified per ASTM D2732 on every production campaign. For automatic packaging lines, the shrink film is printed with solvent-based inks, and surface corona treatment is maintained at 38–42 mN/m. A dyne level below 36 mN/m leads to ink delamination in transit, which has been observed as a batch failure in humid coastal shipping conditions.
Where reverse-printed BOPP laminates require low-temperature sealing of metallised or AlOx-coated substrates, RP129K is coextruded as the exposed sealant layer in 20–30 µm cast films that are subsequently laminated to 18–20 µm BOPP with solventless polyurethane adhesives. The cast sealant film may be corona-treated on the lamination side to 36–40 mN/m and left untreated on the seal side to avoid blocking. Under ASTM F88/F88M, the terpolymer sealant gives 6–10 N/25 mm after lamination, with seal initiation at 105–115 °C. Because the metallised BOPP substrate imposes a heat-sensitivity constraint, the ability to seal the package at 120–130 °C instead of 145–155 °C prevents the vacuum-metallised aluminium layer from developing crazing. The lamination bond strength under ASTM D1876 is typically 2.5–4.0 N/15 mm, and the failure should be film tear or adhesive transfer rather than sealant peel. Storage of the laminated roll at 30–35 °C for 48 h is required to complete solventless adhesive curing; the sealant layer must resist blocking under roll pressure up to 6,000 N. Operators report blocking can occur if the terpolymer cast film has a surface roughness below 0.3 µm Ra and the roll is wound above 0.5 N/mm tension. The addition of 1,000–1,500 ppm synthetic silica as antiblock with a particle size d50 of 4–6 µm and 600–900 ppm erucamide slip is typical; higher levels above 2,500 ppm silica raise haze above 3.0% and reduce seal strength to 5–7 N/25 mm.
Medical device pouches and pharmaceutical cold-form lidding use RP129K in the inner web to seal to uncoated or lacquered Tyvek or medical paper under ethylene oxide or gamma irradiation. The head space of the final pouch must maintain a seal strength of 1.5–2.5 N/25 mm per ASTM F88/F88M after EO sterilisation at 55 °C and 40–60% RH for not less than 4 h. The terpolymer softens during EO exposure but does not crosslink; after aeration for 12–24 h at 40 °C, the seal remains peelable. In gamma-irradiated packages at a dose of 25–50 kGy, propylene-ethylene-butene terpolymer shows a slight increase in seal initiation of 2–4 °C and a reduction in elongation at break of 10–20% due to oxidative chain scission. The packaging structure commonly runs as a 50–70 µm sealant film laminated to a 12 µm polyester outer web. The upstream film line must avoid processing temperatures above 255 °C because the resulting low-molecular-weight oxidation products can migrate and fail extraction limits. The sealant layer may be formulated with a non-aminic stabiliser package; amine-based additives should be avoided because they can interfere with EO residuals and discoloration. The heat-seal die on a blister lidding line is set to 130–145 °C with a 0.8–1.2 s dwell and 0.4 MPa pressure, producing a peelable seal with a clean fiber-tear pattern on Tyvek at 1.5–2.5 N/15 mm. Over-drying or long residence time at high temperature degrades the terpolymer and the seal becomes brittle; a maximum pre-drying condition of 80 °C for 2 h in a desiccant dryer with a dew point below −30 °C is sufficient. Because this grade has low moisture absorption below 0.05% by weight, pre-drying is not normally required unless opened bags have been stored above 60% RH for more than 72 h.
| Reference | Scope | Test method or condition |
|---|---|---|
| US FDA 21 CFR §177.1520 | Olefin polymers for food-contact articles | Extraction testing per §177.1520(d); end-test on final packaging |
| EU Regulation (EU) No 10/2011 | Plastic food-contact material | Overall migration <10 mg/dm²; simulant selection per Annex III |
| USP <661.1> | Plastic packaging for pharmaceuticals | Physicochemical tests; extraction with pH 3 buffer, pH 10 buffer, isopropanol |
| USP <87> | Biological reactivity in vitro | Agar diffusion and elution tests |
| ISO 10993-5 | Medical device biocompatibility | Cytotoxicity of final device, not neat resin |
For clear A/B/A extruded sheet used in shallow thermoforming trays, RP129K is placed in the outer cap layers at 10–15% of total sheet thickness to improve gloss and reduce the plug-assist temperature. The core layer may be a propylene homopolymer with a melt flow rate of 2.0–4.0 g/10 min under ISO 1133-1:2022. Sheet extrusion through a flat die at 230–250 °C onto a roll stack set at 30–45 °C yields a sheet thickness of 300–800 µm. During thermoforming, the terpolymer cap layer lowers the forming temperature by 10–15 °C relative to a homopolymer-only sheet, allowing the use of a forming station set at 150–170 °C. Haze measured per ASTM D1003 on a 400 µm sheet is below 3.0%, and gloss per ASTM D2457 at 60° exceeds 85 GU. However, the terpolymer cap layer reduces the heat deflection temperature of the finished tray; the tray should not be exposed to hot-fill temperatures above 80 °C or microwave reheating above 90 °C unless the core layer provides sufficient thermal resistance. In stationery lamination and photo-album overlay applications, thin cast or blown RP129K film at 20–30 µm is laminated to printed paper at 100–120 °C through a pair of polished steel rolls with a nip pressure of 3–5 N/mm. The low seal initiation allows dry lamination to bleached kraft without activating the paper’s clay coating. The bond strength measured by a 90° peel test under ASTM D6862 is 3–5 N/15 mm, and the failure is usually paper fiber tear. If the nip temperature exceeds 135 °C, the film becomes tacky and wraps the heated roll; a release-coated roll surface with a roughness below 0.2 µm Ra and silicone rubber backup roll of 60–70 Shore A is required.
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Jampilen PP Terpolymer RP129K is supplied as a pelletized propylene-based terpolymer intended for cast film, blown film, biaxially oriented polypropylene heat-seal layers, and thin-wall food-contact packaging. The grade is characterized by a controlled melt flow rate, reduced crystalline melting point, and lower heat-seal initiation temperature than conventional polypropylene random copolymers of equivalent melt flow rate. Published datasheet values list a nominal melt flow rate of 5.0 g/10 min under ISO 1133-1:2022 at 230 °C/2.16 kg, density of 0.900 g/cm³ under ISO 1183-1:2019, tensile stress at yield of 24.0 MPa under ISO 527-2:2012, flexural modulus of 850 MPa under ISO 178:2019, and Vicat softening temperature of 120 °C under ISO 306:2022. The key functional difference from standard random copolymer grades is the displacement of the seal initiation temperature toward 108–112 °C and retention of low haze in quenched films; the trade-off is a reduction in elevated-temperature stiffness and a narrower processing window in high-shear extrusion.
In multilayer BOPP and cast polypropylene structures, the sealant web is required to form a hermetic fin seal at a minimum temperature before the oriented core layer begins to shrink or distort. Seal initiation temperature is defined as the temperature at which a seal strength of 0.5 N/15 mm is reached under a defined dwell force and time in accordance with ASTM F1921-20. For Jampilen RP129K, converter specifications commonly reference a seal initiation temperature of 108 °C; a random copolymer of similar melt flow rate typically initiates sealing at 120–125 °C. The reduction allows vertical form-fill-seal line speed increases of 10–15% when the seal jaw dwell is fixed, because the same seal strength develops at lower jaw temperature or shorter contact time. The lower seal initiation temperature results from reduced crystal order: comonomer units in the propylene chain shorten the average isotactic sequence length, lowering the melting endotherm peak and broadening the melting range between 90 °C and 135 °C as measured by differential scanning calorimetry under ISO 3146:2022.
The melt is processed on cast film lines with single-screw extruders of L/D 25:1 to 30:1 and barrier-type screws. Barrel temperature settings are typically profiled from 180 °C in the feed section to 220–235 °C at the metering zone, with the flat die maintained at 230–240 °C. The shear viscosity of RP129K is lower than that of a homopolymer of the same nominal melt flow rate, which reduces extruder head pressure but increases the risk of melt film instability at gauges below 25 µm. At screw speeds above 80 min⁻¹ on a 75 mm extruder, frictional heating can raise melt temperature above 250 °C, initiating chain scission, gel formation, and loss of seal strength. Melt temperature is therefore maintained at 235–245 °C, and regrind is limited to 20% by weight for monolayer cast film unless lot-by-lot gel evaluation and filtration through a 100 mesh screen pack are used. The grade is not hygroscopic, but storage above 60% relative humidity can increase surface moisture on cold pellets; hopper drying at 80 °C for 2 h prevents surface defects at the die lip.
The following representative values are drawn from the manufacturer’s published technical data sheet and are not batch-release specifications. Users should request the current certificate of analysis for exact lot values.
| Property | Typical value | Test method |
|---|---|---|
| Melt flow rate | 5.0 g/10 min at 230 °C/2.16 kg | ISO 1133-1:2022 |
| Density | 0.900 g/cm³ | ISO 1183-1:2019 |
| Tensile stress at yield | 24.0 MPa | ISO 527-2:2012 |
| Tensile strain at yield | 10% | ISO 527-2:2012 |
| Flexural modulus | 850 MPa | ISO 178:2019 |
| Charpy notched impact, 23 °C | 6.5 kJ/m² | ISO 179-1:2010 |
| Vicat softening temperature, A50 | 120 °C | ISO 306:2022 |
| Melting temperature, DSC | 130 °C | ISO 3146:2022 |
| Haze on 50 µm cast film | 1.5% | ASTM D1003-21 |
| Gloss at 60° | 85 GU | ASTM D2457-21 |
In biaxially oriented film production, the terpolymer is placed in the sealable skin layer of a three-layer or five-layer coextrusion. The core layer is typically a homopolymer with a melting point near 160 °C; the skin layer is coextruded at a thickness between 0.5 µm and 1.5 µm after orientation. Orientation oven temperatures for terpolymer-containing structures are usually set 5–8 °C lower in the transverse direction than for homopolymer skins because the terpolymer skin begins to stretch at lower yield stress. Corona treatment is applied to maintain surface energy above 38 mN/m for lamination or printing adhesion. The final film haze of a 20 µm BOPP substrate with RP129K skins is reported at 1.0–1.5% under ASTM D1003-21, while gloss at 60° is above 85 GU under ASTM D2457-21. The low melting point increases blocking tendency on reels stored above 35 °C; antiblock masterbatch is recommended at 1000–1500 ppm in the skin layer, subject to taste-and-odor requirements for direct food contact.
The selection decision is governed by the balance between seal performance and mechanical rigidity. The terpolymer grade provides a lower seal initiation temperature and improved impact response but sacrifices flexural modulus and Vicat softening temperature relative to a random copolymer of similar melt flow rate. The comparison is most informative when test specimens are conditioned under ISO 291:2008 at 23 °C and 50% relative humidity.
| Property | RP129K terpolymer | Random copolymer, similar MFR | Test method |
|---|---|---|---|
| Seal initiation temperature | 108 °C | 122 °C | ASTM F1921-20 |
| Tensile modulus | 750 MPa | 900 MPa | ISO 527-2:2012 |
| Charpy notched impact, 23 °C | 6.5 kJ/m² | 4.0 kJ/m² | ISO 179-1:2010 |
| Haze on 50 µm cast film | 1.2% | 2.0% | ASTM D1003-21 |
| Vicat softening temperature, A50 | 118 °C | 128 °C | ISO 306:2022 |
In transparent thin-wall injection moulding, RP129K can be used for caps, closures, and medical or cosmetic packaging requiring low residual stress and good contact clarity. Mould temperatures between 15 °C and 30 °C are applied with short hold-pressure profiles; the lower crystallization rate reduces sink marks but requires longer cooling time than homopolymer grades. Published data for this specific configuration is limited, so cavity-specific shrinkage trials are required before tooling release. Moisture content above 0.05% by weight can produce splay and silver streaking on moulded parts, particularly with regrind processed in humid environments.
Jampilen PP Terpolymer RP129K is positioned for direct food-contact applications where the converter must verify compliance under applicable regional legislation. Olefin polymers used in food-contact films are commonly assessed under FDA 21 CFR 177.1520 in the United States and under Regulation (EU) No 10/2011 in the European Union, including specific migration limits for total migration and individual comonomer-derived species. Because the terpolymer contains comonomers beyond propylene, migration testing must consider the relevant comonomer-specific migration limits and residual catalyst or donor residues. REACH and RoHS declarations are typically obtained from the supplier for electrical or durable goods packaging; these do not replace food-contact documentation. Converters should not infer that a single compliance certificate covers all export jurisdictions, because additive packages, masterbatches, and surface treatment levels can alter the final article classification.
In lamination and pouch converting, RP129K is used as the sealant web where low-temperature sealability, clarity, and puncture resistance are required. The sealant layer is commonly combined with metallized polyester, biaxially oriented polyamide, or aluminium foil. Hot-tack performance under ASTM F1921-20 is evaluated at a dwell time of 0.5 s and jaw pressure of 0.3 MPa; terpolymer-based sealants retain measurable hot-tack strength at sealing bar temperatures 10–15 °C below random copolymer references. Seal-through-contamination performance is limited and should not be assumed for powders or liquid-filled sealing because the low seal initiation temperature does not compensate for poor jaw geometry or insufficient dwell force. Batch-to-batch variance in melt flow rate beyond ±0.5 g/10 min can shift screw motor load and seal jaw temperature settings; incoming resin batches should therefore be checked for melt flow rate and seal initiation temperature before large-scale pouch campaigns.