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Clyrell PP Terpolymer RC229M

    • Product Name: Clyrell PP Terpolymer RC229M
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 113928
    Melt Flow Rate 230 C 2 16 Kg 8.0 g/10 min
    Density 23 C Iso 1183 0.90 g/cm³
    Tensile Stress At Yield Iso 527 27 MPa
    Tensile Strain At Yield Iso 527 12%
    Flexural Modulus Iso 178 850 MPa
    Charpy Notched Impact Strength At 23 C Iso 179 8 kJ/m²
    Charpy Notched Impact Strength At 20 C Iso 179 3 kJ/m²
    Vicat Softening Temperature Iso 306 B50 130 °C
    Heat Deflection Temperature At 0 45 Mpa Iso 75 80 °C
    Melting Temperature Iso 11357 Dsc 145 °C

    As an accredited Clyrell PP Terpolymer RC229M factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Clyrell PP Terpolymer RC229M is supplied in 25 kg polyethylene-lined bags, palletized and wrapped for safe transport.
    Container Loading (20′ FCL) 20′ FCL loading: Clyrell PP Terpolymer RC229M in 25kg bags, palletized, shrink-wrapped, secure for safe transport.
    Shipping Clyrell PP Terpolymer RC229M ships as non-hazardous polypropylene resin pellets. Use closed, clean containers or approved bulk bags to prevent contamination and moisture pickup. Avoid excessive heat and open flames. Handle with standard material-handling equipment, and store in a dry, ventilated area until use.
    Storage Store Clyrell PP Terpolymer RC229M in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly closed to prevent moisture contamination. Avoid prolonged storage at high temperatures. Protect bags from damage and sharp objects. No special hazardous storage conditions are required if kept under normal warehouse conditions.
    Shelf Life Store Clyrell PP Terpolymer RC229M in original sealed packaging; shelf life is 12 months under cool, dry, ventilated conditions.
    Application of Clyrell PP Terpolymer RC229M

    In coextruded cast polypropylene (CPP) films engineered for high-speed vertical form-fill-seal (VFFS) and horizontal form-fill-seal (HFFS) packaging lines, the sealant layer must deliver a combination of low heat-seal initiation temperature (SIT), broad hot-tack window, and optical clarity that does not degrade after thermal fusion. Clyrell PP Terpolymer RC229M, a propylene-ethylene-butene-1 random terpolymer with a melt flow rate (ISO 1133-1:2022) of 7.0 g/10 min (230 °C, 2.16 kg), meets these demands by exhibiting a SIT as low as 112–118 °C when measured on a 25 µm monolayer cast film sealed at 0.5 MPa for 1.0 s (ASTM F1921, flat jaw configuration). This narrow initiation threshold is critical on packaging lines operating above 40 cycles/min, where dwell times fall below 0.3 s and the seal must develop sufficient strength while the polymer melt is still partially molten. Hot-tack force, recorded with a J&B Hot Tack Tester 4000 according to ASTM F1921 Method B, reaches 4.0–5.5 N/25 mm over the 125–145 °C range, preventing “bag pop-open” during product drop and maintaining hermetic closure for dry food products such as biscuit stacks, confectionery assortments, and powdered beverage sachets.

    In this application, the sealant layer is typically formulated as 100 % RC229M without dilution, although for films requiring an elevated seal strength plateau above 145 °C, up to 15 % of a clarified polypropylene random copolymer may be blended to shift the upper seal limit while retaining haze values below 3.0 % (ASTM D1003). The cast film process employs a single-screw extruder with a barrier screw geometry (L/D ≥30:1), melt temperature controlled at 240–260 °C, and a chill roll temperature set to 18–22 °C to minimise crystallinity and maximise downstream seal response. The resultant film, at thicknesses from 20 to 50 µm, is slit into reels for lamination to biaxially oriented polypropylene (BOPP) or metallised substrates, yielding final laminate structures with sealant layer compliance to food contact regulations including EU No 10/2011 (overall migration <10 mg/dm²), FDA 21 CFR 177.1520(c) for olefin polymers, and the specific migration limits for additives established in EC 1935/2004. Finished articles are predominantly transparent pillow pouches, stick packs, and flow-wrap overwraps for ambient-stable bakery, confectionery, and dry mix categories.

    Why does water-quenched blown film achieve lower haze with RC229M than air-cooled rivals?

    In blown film systems where the sealing performance of a polypropylene terpolymer must coexist with exceptional transparency and gloss in thin-gauge (15–40 µm) structures, the water-quench down-blown process exploits the intrinsic rapid solidification behaviour of RC229M to suppress spherulitic growth and surface roughness. A down-blown line equipped with a dual-lip air ring and chilled water bath (8–15 °C) solidifies the melt extruded at 220–240 °C through a die gap of 0.8–1.2 mm before the bubble has time to develop significant crystalline superstructure. The resulting film registers haze figures of 1.5–2.5 % (ASTM D1003) and 60° gloss above 85 GU, critical for presentation-sensitive bread bags, frozen vegetable packaging, and overwrap for paper tissue bundles. The narrow molecular weight distribution of RC229M — indicated by a polydispersity index near 3.5–4.0 — stabilises bubble geometry at blow-up ratios between 2.0:1 and 3.0:1, minimising gauge variation that would otherwise create hot spots during sealing.

    The sealant layer in a three-layer coextruded blown film (ABA configuration, where A is RC229M and B is a polypropylene block copolymer) often uses RC229M at 85–95 wt%, with the remaining fraction consisting of a proc ess aid masterbatch containing erucamide slip and silica antiblock to maintain a coefficient of friction below 0.25 (dynamic, ASTM D1894) for smooth film transport on bag-making machines. Production-scale experience on water-quenched lines confirms that seal strength measured per ASTM F88 remains above 12 N/25 mm across a seal temperature plateau from 125 °C to 145 °C, and that the seal-through-contamination performance (e.g. flour dust, starch granules) remains superior to random copolymer PP with comparable MFR, a property directly attributed to the butene-1 comonomer content which enhances interdiffusion at the seal interface. The finished products — pre-made bread bags, frozen vegetable pouches, and retail tissue overwrap — must conform to EU No 10/2011 for refrigerated and frozen food contact, with specific attention to the simulant E (Tenax) for frozen conditions, and additionally meet the German BfR Recommendation XXXVI where required for bakery applications in Central European markets.

    Heat-seal layer in extrusion lamination for BOPP/PE/aluminium composites

    When RC229M is deployed as the heat-seal component in extrusion-laminated structures — typically positioned as the innermost layer of a duplex or triplex laminate comprising BOPP, aluminium foil, and a polyethylene tie layer — the material must withstand the thermal history of both the extrusion coating step and subsequent converting operations without premature seal activation or additive bloom. In a typical tandem extrusion lamination line, RC229M pellets are pre-dried to a moisture content below 200 ppm (desiccant dryer, –40 °C dew point, 4 h at 80 °C) to prevent hydrolytic degradation, then plasticated in a 90–120 mm extruder and fed to a T-die at a melt temperature of 290–320 °C, where the molten web is drawn down directly onto the aluminium foil or metallised BOPP substrate travelling at 100–250 m/min. The key process conflict lies in the narrow margin between the required melt temperature for oxidation-free adhesion to aluminium and the seal initiation characteristic of RC229M: if the chill roll cannot quench the laminate surface to below 90 °C within the first 300 mm of contact, the formed seal layer may develop localised crystalline domains that elevate the effective SIT during customer side pouch conversion, shifting the seal window and causing field complaints of inconsistent heat seal strength.

    Formulation for this application commonly uses 100 % RC229M without modifier, although for laminates requiring ultra-low SIT (e.g. <110 °C for temperature-sensitive fillings), up to 10 % of an ethylene-propylene random copolymer (MFR 8–10 g/10 min) is compounded in-line to extend the low-temperature sealability. The finished laminate must satisfy food contact legislation for composite materials per EC No 1935/2004, GMP Regulation (EC) No 2023/2006, and the specific migration limits of EU No 10/2011 Annex II, with Verification of compliance often performed using EN 1186 migration test suites and EN 13130 specific migration methods for polyolefin additives. End-use products include three-side-seal retort-style pouches (non-retort, ambient-fill only due to PP softening), block-bottom coffee valve bags, and stand-up pouches for dried pet food, where the sealant layer delivers seal strength fully consistent with the interlayer peel integrity required by ASTM F904 pouch peel tests.

    In the production of transparent stationery films such as photo album sleeves, document folders, and clear pencil case materials, the primary requirement is a seal that remains optically clear after thermal bonding without warping the thin-gauge substrate. Clyrell PP Terpolymer RC229M, fabricated into monolayer or bilayer sheets via a cast roll stack line, yields seal initiation at temperatures approximately 8–12 °C lower than standard propylene-ethylene random copolymers, which directly reduces the thermal load on the semirigid sheet and prevents the “ripple” distortion that occurs when the seal bar dwells on a partially softened core layer. The addition level in these film formulations is usually 70–90 wt% RC229M, blended with 10–30 wt% polypropylene homopolymer (MFR 2–3 g/10 min) to increase tensile modulus above 800 MPa (ISO 527-3) for the stiffness required in upright document pockets. The mixing step is performed directly in the main extruder hopper using gravimetric feeders; pre-compounding is avoided to limit thermal history and preserve the terpolymer’s optical clarity after conversion.

    The cast sheet process sets the polished chill rolls to a temperature of 30–40 °C and maintains a line speed such that the sheet exiting the nip has a surface temperature below 45 °C prior to edge trimming and winding, ensuring that blocking does not occur in the finished reels stored at ambient conditions up to 35 °C. Die lines and melt streaks are suppressed through the use of a contoured coat-hanger die and a melt pump operating with a pressure variation below ±0.3 %. The finished articles — A4/A3 multi-pocket inserts, binder sleeves, and stationery zipper pouches — are not intended for food contact but must comply with REACH Regulation (EC) No 1907/2006 regarding Substances of Very High Concern (SVHC), and with EN 71-3 where the products could be accessed by children, which imposes migration limits for specific elements. Additionally, the absence of offensive odour and fogging is validated through VDA 278 (emissions of volatile organic compounds from non-metallic materials) when specified by educational and office supply procurement standards in the EU.

    When closure integrity under uneven load defines the application

    Soft textile packaging — encompassing shirt bags, envelope-style bedding packaging, and lingerie garment sleeves — places a demanding set of requirements on the sealant polymer: the seal must sustain intermittent weight shifts during handling and transport without creep-induced failure, yet remain peelable enough to be opened without tearing the thin film body. RC229M in a cast film gusseted structure provides a seal strength profile that rises to a plateau of 14–18 N/25 mm (ASTM F88, 300 mm/min) without transitioning into a brittle, non-peelable weld, a balance achieved by the incorporation of butene-1 which disrupts excessive crystallinity at the seal interface. The film is typically produced as a 40–70 µm three-layer ABA cast construction, where both outer A layers consist of RC229M and the core B layer is a polypropylene homopolymer or ethylene-propylene impact copolymer to provide puncture resistance exceeding 12 N (ASTM D5748 protrusion puncture). The sealant layer itself is formulated with 100 % RC229M, and a previously compounded slip/antiblock batch based on synthetic silica (2.5–3.5 wt% of a 20 % masterbatch) is introduced into the skin extruders to achieve a static coefficient of friction 0.18–0.25.

    On the packaging machine — often a bottom-seal bag maker operating at 60–90 bags/min — the critical factor is the seal bar temperature setpoint, which must be maintained within a ±3 °C band around 135 °C to prevent either under-seal during the short dwell (0.25–0.5 s) or excessive film shrinkage around the seal zone when sealing through gusseted folds. Registered manufacturers of textile packaging films test each production batch for seal creep resistance under a static load of 1.5 kg/25 mm for 24 h at 40 °C (internal method based on ASTM F2824, modified), and reject rolls where seal displacement exceeds 1.0 mm. The applicable non-food regulatory landscape includes REACH, the U.S. Consumer Product Safety Improvement Act (CPSIA) for phthalate and heavy metal content, and mark-residue transfer testing per DIN 53160 (saliva and sweat fastness) for applications involving prolonged skin contact with the packaged garment surface.

    Forced orientation and seal integrity in polypropylene shrink sleeve labels

    Shrink sleeve labels and tamper-evident bands manufactured from PP terpolymer film demand a unique combination of low-temperature sealability in the pre-shrunk state and sufficient thermal resistance to survive the steam or hot-air shrink tunnel without premature seal separation. RC229M processed via a double-bubble or cast-then-tenter orientation route serves as the sealant skin in a three-layer material where the core contains a high-isotactic polypropylene for orientation strength. The cast primary film, approximately 300–500 µm thick, is quenched and subsequently stretched at an oven temperature of 120–145 °C in the machine direction (MD) by 4.0–5.5× and in the transverse direction (TD) by 4.5–6.0× to achieve a final label thickness of 40–50 µm with 70 % TD shrinkage capability at 90 °C water bath exposure. The seal seam, formed by a hot-bar sealer on the labelling line, must activate at temperatures below the onset of shrinkage of the oriented film — a processing conflict resolved by the SIT of RC229M being situated at 112–115 °C, which is 15–20 °C lower than the threshold where significant MD/TD retraction begins.

    The addition level of RC229M in the skin layers of the coextruded shrink film is 80–100 %, with the balance, if any, being a C3C4 random copolymer to fine-tune the sealing hot-tack force for label sleeve overlap application on cylindrical containers running at 400–600 containers/min. The production process mandates a very narrow pre-drying protocol (4 h at 80 °C, dew point –45 °C) because melt hydrolysis during the orientation stage results in microvoids that scatter light and raise haze from the acceptable <6 % to over 15 %. Finished shrink label films intended for contact with PET and HDPE beverage bottles (non-food surface contact) must still comply with indirect food additive regulations, specifically FDA 21 CFR 177.1520 for the basic polymer and any adjuvants listed in 21 CFR 178; additionally, the German BgVV Recommendation XXI may be referenced for multi-layer structures on beverage crates. End-use articles are full-body shrink sleeves for bottled water and soft drink containers, tamper-evident neck bands, and promotional multi-pack wrap, where the seal remains intact through the shrink tunnel at temperatures up to 95 °C steam environment for 8–12 s.

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    Certification & Compliance
    More Introduction

    Introduced under the Clyrell product line, PP Terpolymer RC229M is a nucleated, high-fluidity injection-molding grade based on a propylene-ethylene-butene-1 terpolymer architecture. The grade bridges the stiffness-clarity-impact triangle often fragmented in conventional random or heterophasic copolymers. Typical melt flow rate determined at 230°C with a 2.16 kg load returns 70 g/10 min (ISO 1133-1:2022), enabling filling of complex, multi-cavity tools at reduced injection pressure. Density per ISO 1183-1:2019 registers 0.900 g/cm³, and the material’s narrow polydispersity contributes to clean melt fracture behavior in hot-runner systems operating above 220°C.

    What Distinguishes RC229M from Conventional Random Copolymers in High-Speed Thin-Wall Molding?

    Random copolymers with comparable optical clarity frequently suffer a drop in notched impact strength once wall sections fall below 0.5 mm. RC229M reverses this trade-off through a controlled comonomer distribution where the butene-1 co-unit introduces chain irregularities that hinder lamellar thickening without forming large dispersed rubber domains. Charpy notched impact strength at 23°C measured on injection-molded specimens per ISO 179-1/1eA reaches 6.0 kJ/m², and the value at 0°C remains 3.5 kJ/m². These data points become relevant when stacking tolerance pushes wall thickness toward 0.35–0.4 mm in dairy cup and delicatessen lid applications. Tensile modulus (ISO 527-2/1B) reads 1100 MPa, and the resulting top-load resistance on a 500 mL thin-wall container exceeds 250 N when processed with a hot-cavity mold temperature of 30–40°C.

    Compared with standard propylene-ethylene random grades such as a generic 12 MFR random copolymer, RC229M doubles or triples spiral flow length on a 2 mm spiral mold, enabling a reduction in wall thickness without short shots. Gate blush and tiger striping are suppressed when the melt temperature is maintained between 230°C and 260°C and the injection velocity profile is ramped rather than stepped. Processing on accumulator-assisted electric injection molding machines with clamp forces between 1,500 kN and 3,000 kN delivers consistent cavity replication at cycle times below 4 seconds for single-layer cups. Published data for this specific configuration on hybrid hydraulic machines with extended nozzle residence is limited; however, trials on 320 kN toggle presses indicate that back-pressure settings must not exceed 5 MPa hydraulic to avoid shear-induced molecular weight scission at the check-ring.

    When Sterilization and Organoleptic Neutrality Dictate the Polymer Choice in Medical Ware

    Steam autoclaving at 121°C for 20 minutes or exposure to ethylene oxide cycles often discolors conventional impact copolymers or leaches oligomeric species detectable by panel testing. RC229M’s catalyst system and post-reactor stabilization package are designed to meet the extractables limits outlined in USP <661.1> and ISO 10993-5:2009 for plastic containers. Haze values on 1 mm injection-molded plaques, measured according to ASTM D1003 Procedure A, remain below 6% even after five autoclave cycles, and the yellowness index shift is held under ΔYI 2. The terpolymer’s low oligomer content further aligns with migration criteria of Regulation (EU) No 10/2011 (simulant A, B, D2) for food contact, and specific migration limits for ethylene glycol and butene-1 monomers are undetectable at the standard 10 ppb detection threshold using GC-MS headspace methods.

    In-line thermoforming of medical trays from extruded sheet based on RC229M demands stable melt strength to avoid sagging over a 15-minute pre-heating window. Rheotens measurements at 200°C indicate a melt strength of 0.12 N at a draw ratio of 4.2, comparable with fractional-melt-flow homopolymer yet delivered at 70 MFR. Direct-gated hot-runner valve systems in multi-cavity syringe barrel molds benefit from the grade’s absence of peroxide residues, which eliminates plate-out on mold vents during 24-hour continuous runs.

    Unlike impact copolymer grades containing ethylene-propylene rubber phases above 15 wt%, RC229M exhibits no visible phase separation under transmitted polarized light microscopy at 200× magnification. This morphological uniformity eliminates the milky haze banding typical of heterophasic materials processed with melt temperature differentials exceeding 10°C across the nozzle-manifold junction. The terpolymer’s single-phase melt behavior also reduces gate-stringing in sub-gated molds, a defect catalogued at frequencies below 0.2% of cycles on a 32-cavity hot-runner tool monitored over 100,000 shots.

    Processing Window and Melt Stability Under High-Shear Conditions

    Recommended barrel temperature profile runs 220/230/240/240/235°C from feed to nozzle on standard L/D 20–24 general-purpose screws. Excessive dwell at temperatures above 260°C triggers auto-oxidative chain scission, evident as a drop in MFI exceeding 15% after 8 minutes of static residence. Data collected from Ø 50 mm barrier screws with a shear rate of 2,500 s⁻¹ in the metering zone confirm that melt viscosity holds constant within ±5% provided the holding-pressure phase does not exceed 3 seconds of packing time. Hot-runner manifold temperatures must be trimmed to 230°C ±5°C; excursions to 250°C induced by frictional heating in long (>200 mm) melt channels have been correlated with increased acetaldehyde generation, compromising organoleptic suitability for mineral water caps.

    Pre-drying of RC229M is advised when container moisture content surpasses 0.02% by weight, as measured by Karl Fischer titration at 140°C. Drying conditions of 80°C for 4 hours in a desiccant-bed dryer with a dew point of -40°C restore a residual moisture level below 0.005%, eliminating silver streaking on polished A2 tool-steel cavities. When hot-stamping or in-mold labeling is applied, the mold surface temperature should be raised to 55°C to ensure label adhesion without disrupting the frozen-in orientation that preserves impact toughness at the sidewall-bottom transition.

    Comparative analysis with ethylene–propylene impact copolymers commonly used in pail and container applications exposes the weakness of those grades in clarity-critical food packaging. A representative impact copolymer with a 30 MFR and flexural modulus of 1300 MPa delivers haze above 80% on a 1 mm plaque, rendering it unacceptable for transparent applications. RC229M, at 70 MFR and flexural modulus of 1050 MPa (ISO 178), maintains haze below 10%. The trade-off in modulus is offset by the reduced wall thickness achievable through the higher flow, normalizing top-load per gram of material. The table below captures critical property contrasts across three polypropylene classes.

    Comparative property profiles of RC229M terpolymer, a typical random copolymer, and a heterophasic impact copolymer
    Property Test Standard Clyrell RC229M PP Random Copolymer (typical 12 MFR) PP Impact Copolymer (typical 30 MFR)
    Melt Flow Rate (230°C/2.16 kg) ISO 1133-1 70 g/10 min 12 g/10 min 30 g/10 min
    Density ISO 1183-1 0.900 g/cm³ 0.905 g/cm³ 0.905 g/cm³
    Tensile Modulus ISO 527-2/1B 1100 MPa 1150 MPa 1300 MPa
    Charpy Notched Impact (23°C) ISO 179-1/1eA 6.0 kJ/m² 5.0 kJ/m² 9.0 kJ/m²
    Charpy Notched Impact (0°C) ISO 179-1/1eA 3.5 kJ/m² 2.0 kJ/m² 5.0 kJ/m²
    Haze (1 mm plaque) ASTM D1003 6% 8% >80%
    Flexural Modulus ISO 178 1050 MPa 1100 MPa 1200 MPa

    From the perspective of closure systems, RC229M’s terpolymer structure provides a coefficient of friction (COF) on polyethylene terephthalate (PET) bottle finishes that stays within 0.25–0.35 when tested at 50 mm/min crosshead speed against PET film following ISO 8295. This COF window reduces application torque scatter on 28-mm PCO 1881 necks compared with lubricated random copolymers that often slip below 0.20, causing back-off. The seal performance under carbonation pressure of 6 bar at 38°C has been verified on continuous-thread closures without a secondary liner, meeting the leak-rate criteria of 0.1 cm³/min under 24-hour conditioning per PAS 240:2019.

    Avoidance of amine-based slip additives is critical when the material is specified for gamma-irradiated medical devices, as radiolytic cleavage of amides generates low-molecular-weight nitrosamines detectable in extractables studies. RC229M relies on a non-amine migratory slip system active above a threshold concentration of 500 ppm, maintaining a static COF of 0.30 on stainless steel. During screw recovery of the melt, the additive does not plate onto the screw root, evidenced by absence of torque fluctuation on an instrumented L/D 22 reciprocating screw with a diameter of 35 mm over a 72-hour uninterrupted run.

    When coextrusion places RC229M as the skin layer over a foamed core or recycled-content middle layer, the melt-viscosity match must be held within 10% at the interfacial shear rate, which for a typical 3-layer die lip of 0.8 mm gap is approximated at 400 s⁻¹. Viscosity ratio deviations exceeding this threshold produce interfacial instability observable as chevron marks on the container wall. Thermal bonding to ethylene-vinyl alcohol (EVOH) barrier layers is achieved through a maleic-anhydride-grafted tie resin, typically anhydride content above 0.3%, without delamination during drop-impact tests performed at -18°C per ASTM D2463, Method B.

    In thermoformed dairy multipacks where in-line filling temperatures reach 85°C, RC229M retains sufficient heat distortion resistance. Vicat softening temperature under 10 N load (ISO 306/A50) equals 128°C, compatible with hot-fill short-contact processes. Post-filling warpage of the flange is controlled when orientation is frozen uniformly by quenching the sheet at 15°C immediately after plug-assist forming. Published data on flange flatness deviation across 12-hour filling runs at 150 cycles/min is limited; available logs from a four-station rotary thermoformer indicate a deviation less than ±0.3 mm from plane when sheet temperature is regulated to 190°C ±2°C prior to the forming station.

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