| HS Code | 281112 |
| Product Name | NOVARES PURE 1120 |
| Resin Type | Hydrogenated C9 Hydrocarbon Resin |
| Application | BOPP Films |
| Softening Point Ring Ball | 112 °C |
| Color Gardner | <1 |
| Acid Value | <1 mg KOH/g |
| Melt Viscosity At 190 C | 520 mPa·s |
| Density At 20 C | 1.06 g/cm³ |
| Glass Transition Temperature Tg | 55 °C |
| Refractive Index At 20 C | 1.51 |
| Bromine Number | <1 g Br/100g |
| Tga 5 Weight Loss Temperature | ~250 °C |
As an accredited NOVARES PURE 1120 Hydrogenated C9 Resin for BOPP Films factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | NOVARES PURE 1120 Hydrogenated C9 Resin is packaged as solid pellets in 25 kg multi-wall paper bags for BOPP film applications. |
| Container Loading (20′ FCL) | Load 25kg bags on pallets, shrink-wrapped and secured, stuffed into a 20ft FCL container with proper ventilation and bracing. |
| Shipping | Ship in clean, dry, intact packaging, protected from moisture, direct sunlight, and extreme heat. Store at room temperature away from ignition sources and incompatible materials. Ensure proper labeling, adequate ventilation, and secure loading to prevent bag damage. Use appropriate PPE when handling. Avoid prolonged high-temperature exposure to preserve resin quality. |
| Storage | Store in a cool, dry, well-ventilated area, away from heat, open flames, and direct sunlight. Keep containers tightly sealed to prevent moisture pickup and contamination. Avoid storage above 50°C. Under proper conditions, shelf life is typically 12 months from production date. Follow manufacturer’s safety and handling guidelines. |
| Shelf Life | Shelf life is 2 years when stored in original unopened packaging in a cool, dry place, protected from sunlight and heat. |
Addition of NOVARES PURE 1120 to the core layer of a tenter-stretched BOPP film is performed as an in-line gravimetric blend with PP homopolymer pellets, normally after a 15 min low-speed tumble mixing step to reduce hopper stratification. The resin has a nominal softening point of 120 °C as measured by ASTM E28, and its hydrogenated structure provides a Gardner colour below 1 under ASTM D1544; these two parameters define the dosing window rather than the final film properties. The modified PP enters a single-screw extruder with L/D 30–40, a barrier screw, and a melt pump, where the low-molecular-weight resin reduces pressure drop across the melt filter and permits either a 5–12 °C reduction in melt temperature or a higher screw speed at constant torque, depending on the control strategy of the line. In tenter operations producing 20–40 µm film, the resin is typically evaluated in the range of 3–10 wt% of the core layer; published data for this specific grade under full ISO testing are limited, and converter trials must isolate the resin effect from the β-nucleant or additivation package used in the same layer. Tensile modulus is measured according to ISO 527-3, haze according to ISO 14782, and water vapour transmission rate according to ISO 15106-3; because draw ratio and orientation temperature alter the amorphous phase distribution, the same addition level can shift modulus differently on a sequential longitudinal-then-transverse orientation line compared with a simultaneous stretching line. The resin should be pre-dried at 80 °C for 2 h when silo or day-bin relative humidity exceeds 60 %, because absorbed moisture generates micro-voids and die-lip deposits. Extrusion melt temperature should not exceed 280 °C for a residence time above 8 min; although hydrogenation removes reactive unsaturation, thermal-oxidative yellowing can still occur in the presence of oxygen at the feed throat if the blend is starve-fed unevenly. Above 10 wt%, processing trials on comparable hydrogenated C9 grades have shown an increased tendency to form die-lip build-up and reduced transverse-direction stretch uniformity, which appears as gauge bands on the finished roll.
Coextruded BOPP skin layers are usually based on propylene-ethylene or propylene-butene copolymers with a low seal initiation temperature. If NOVARES PURE 1120 is added to a heat-sealable skin layer, the addition level is kept below 5 wt%, and the development target is usually a lower seal initiation plateau rather than a higher ultimate seal strength. Seal strength after 0.5 s dwell and 2 bar jaw pressure is measured by ASTM F2029; hot tack is measured by ASTM F1921. The hydrogenated C9 resin broadens the onset of interfacial melting but also raises the blocking tendency of the wound roll, especially at storage temperatures above 35 °C. Blocking is evaluated through ASTM D3354 or an internal peel-blocking fixture; coefficient of friction is measured by ASTM D1894. Because the skin layer is only 0.8–2.0 µm thick, the resin concentration at the surface is not equivalent to the bulk formulation; film ageing can concentrate low-molecular-weight species at the outer 10–20 nm through surface segregation, even when the skin layer is not directly modified. Above 5 wt%, blocking becomes difficult to control without increasing anti-block masterbatch silica to 0.5–1.5 wt%, which then raises haze beyond acceptable limits for transparent packaging. If surface energy falls below 38 mN/m after corona treatment, as measured by ASTM D2578 wetting tension fluids, print adhesion on solvent-based flexo inks may fail. Consequently, most converters restrict the resin to the core or tie layer and leave the seal skin unmodified unless a specific hot-tack deficit must be corrected.
In white opaque BOPP label film production, the cavitated core layer contains CaCO3 at 8–15 wt%, often with a β-nucleating package that promotes void formation during sequential stretching. NOVARES PURE 1120 is not used as the cavitation agent itself but as a dispersion modifier at 3–6 wt% in the same layer. The low-viscosity resin wets the mineral surface and reduces the agglomerate size that survives the masterbatch dilution stage; this effect is monitored by filter pressure value, film optical defects under a 500 lux light table, and opacity measured according to ISO 2471. Biaxial stretching of the filled layer at temperatures between 145 °C and 160 °C creates elongated voids whose geometry controls the opacity-to-density trade-off; the resin modifies the elongational viscosity of the PP matrix, allowing the voids to extend without excessive film rupture. The final label film is typically 50–70 µm thick, with a density of 0.65–0.85 g/cm³ depending on draw ratio, and is subsequently corona-treated to 38–42 mN/m under ASTM D2578 for UV flexo or offset printing. Die-lip build-up is the primary failure mode when the resin is overdosed or when the CaCO3 grade contains excessive moisture; pre-drying of the mineral masterbatch at 80 °C for 2 h is standard when ambient relative humidity exceeds 60 %. The grade is not a substitute for the cavitation agent, and reducing CaCO3 below the minimum specified by the masterbatch producer while increasing resin concentration leads to incomplete void formation and an opacity loss that cannot be recovered by additional TiO2.
Metallization trials on BOPP films are conducted in a vacuum chamber at 10^-4 mbar to 10^-5 mbar with aluminium wire feed, producing an optical density of 2.0–3.0 and a deposited layer thickness near 40 nm. The resin-modified core film is evaluated for oxygen transmission rate according to ASTM D3985 at 23 °C and 0 % RH, and water vapour transmission rate according to ASTM F1249 at 38 °C and 90 % RH. A clear metallized barrier improvement is not guaranteed by resin addition alone; the barrier depends on the density of pinholes, surface defects, and oligomer-induced weak boundary layers at the metal-polymer interface. In a three-layer coextrusion, NOVARES PURE 1120 is therefore restricted to the core layer, while the metallizable skin remains an unmodified PP homopolymer or a low-additive metallic skin. If the resin is present in the skin above 2 wt%, corona treatment at 38–42 mN/m cannot compensate for the surface segregation of low-molecular-weight resin, and aluminium anchorage failure appears as metal pick-off during tape pull tests. This is tested internally after metallization with a pressure-sensitive tape method adapted from ASTM D3359, although the method is not specific to metallized film. Process control includes residual gas analysis of the vacuum chamber, because moisture and volatiles released from the film during pump-down suppress adhesion; films containing NOVARES PURE 1120 are therefore held in a low-humidity storage room at 35–40 % RH for 24 h prior to metallization. Published quantitative barrier improvement figures for this specific grade in metallized BOPP are limited; converter trials generally report that the benefit is an improvement in film flatness and drawability rather than a direct drop in oxygen transmission.
The qualification matrix applied to the modified film follows the standards listed below.
| Application layer | Property | Standard | Control condition |
|---|---|---|---|
| Core layer | Melt mass-flow rate | ISO 1133-1:2022 | 230 °C, 2.16 kg |
| Core layer | Haze | ISO 14782 | 24 h conditioning at 23 °C/50 % RH |
| Core layer | Tensile modulus | ISO 527-3 | 200 mm/min crosshead speed |
| Skin layer | Seal strength | ASTM F2029-16 | 150 °C, 0.5 s, 2 bar |
| White label film | Opacity | ISO 2471 | Green filter reflectance |
| Metallized barrier film | Oxygen transmission | ASTM D3985 | 23 °C, 0 % RH |
| Metallized barrier film | Water vapour transmission | ASTM F1249 | 38 °C, 90 % RH |
| Tape backing | Silicone peel adhesion | AFERA 5001 | 180 ° peel angle |
High-speed tobacco overwrap lines running at 300–450 packs/min require a 16–20 µm BOPP film with high stiffness, low elongation, and a neutral odour profile. In this application, NOVARES PURE 1120 is evaluated in the core layer at 3–5 wt% to raise the secant modulus measured by ISO 527-3 and to improve cut-and-fold deadfold on the wrapping stations. The skin layers remain an unmodified sealable PP copolymer to avoid changes in organoleptic performance and to maintain seal integrity at high speed. Odour and sensory carry-over are qualified by DIN 10955:2008; because the overwrap is not in direct contact with tobacco in the sealed pack, the primary concern is volatile transfer into the pack headspace. Process limitations appear when the resin loading exceeds 5 wt% in the core: elongation at break can fall below the level required for the initial fold, and the film may split at the crimp edges on older overwrappers that use reciprocating sealing jaws. Moisture barrier is confirmed by ISO 15106-3, and optical clarity is checked by ISO 14782. For this specific tobacco configuration, published data with NOVARES PURE 1120 are limited; the industrial practice is to run a controlled plant trial using the same batch of resin, PP, and masterbatch that will be used in production, because the sensory threshold is not predicted by physical constants alone.
BOPP pressure-sensitive tape backing in thickness from 30 µm to 50 µm is often a three-layer film with a stiff core and a release- or adhesion-modified skin. NOVARES PURE 1120 at 5–10 wt% in the core raises tensile modulus and reduces elongation under unwind tension, which improves slitting and tape conversion at speeds above 500 m/min. The side to be silicone-coated is corona-treated to 38–44 mN/m as measured by ASTM D2578 before silicone application. Low-molecular-weight hydrocarbon resin that migrates into the skin can create a weak boundary layer that reduces silicone anchorage; this is detected by a rub-off test after solvent extraction and by stable peel adhesion according to AFERA 5001 or FINAT FTM 1. If the resin is inadvertently compounded into the release skin instead of the core, the low-molecular-weight fraction can bloom under warm storage and the silicone layer can delaminate during unwinding. The operational boundary is therefore structural: resin belongs in the core, and release-layer migration must be checked after 30 days at 40 °C. Surface energy decay below 36 mN/m during post-corona ageing is a rejection criterion; inline plasma treatment immediately before silicone coating is sometimes used but does not remove surface-segregated resin already present after film winding. For direct food-contact tape applications, the entire film construction must still meet overall migration below 10 mg/dm² under EN 1186-1, and the specific monomers or additives in the food-contact layer must comply with EU 10/2011; NOVARES PURE 1120 itself is not a direct food-contact layer component unless the film’s migration testing demonstrates compliance.
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NOVARES PURE 1120 Hydrogenated C9 Resin for BOPP Films belongs to the hydrogenated aromatic C9 hydrocarbon resin class produced by catalytic saturation of selected vinyl-aromatic and indene-rich C9 cracker fractions. The product is supplied as a low-molecular-weight, water-white pastille or flake with a nominal ring-and-ball softening point of 112 °C determined in accordance with ASTM E28. In biaxially oriented polypropylene film manufacture, the resin functions as a melt-processable modifier for the PP-rich core or skin layer to alter amorphous-phase mobility, reduce melt viscosity during flat-die extrusion, and modify the wetting tension of corona-treated surfaces after orientation. Typical addition levels referenced in publicly available compounding literature for hydrogenated C9 resins in polypropylene film fall between 5 wt% and 15 wt% of layer mass, although the exact level for a given BOPP formulation is determined by the required sealing, stiffness, optical property, and surface-energy balance. Because the resin is hydrogenated rather than simply heat-polymerised, the concentration of residual aromatic unsaturation is low, which reduces molten Gardner colour to ≤1 when tested according to ASTM D1544 and lowers the quantity of low-molecular-weight volatile aromatic species available to contribute to odour or fuming on tenter-frame lines.
In comparison with standard non-hydrogenated C9 resins, NOVARES PURE 1120 exhibits a narrower molecular weight distribution and a reduced tendency to generate colour bodies during high-temperature film processing. The hydrogenation step also increases thermal stability during extended residence at melt temperatures above 230 °C. The principal operational consequence for BOPP film production is that the resin can be added directly to a PP-rich core layer without the darkening, extractable-rich behaviour, or pronounced fuming commonly associated with conventional aromatic C9 tackifiers. For film convertors, the low acid number and low volatile content reduce the risk of plate-out on casting rolls, die-lip deposit formation, and odour transfer into food-contact films. Published data for this specific configuration is limited for some film-performance endpoints, so converter validation with a defined film structure and tenter-frame orientation conditions remains necessary.
The catalytic hydrogenation of C9 aromatic streams converts indene, vinyl toluene, and related unsaturated species into partially or fully saturated cycloaliphatic structures. This chemical transformation is the key differentiator among the resin classes used in polypropylene film modification. Conventional C9 resins retain a high degree of aromatic unsaturation and typically show molten Gardner colours in the range of 5–10, higher acid numbers, and measurable volatile evolution at 180 °C. C5/C9 copolymers offer intermediate compatibility and colour but generally possess lower upper service temperatures and broader molecular weight distributions unless they are also hydrogenated. NOVARES PURE 1120 is positioned closer to a water-white, thermally stable modifier for polypropylene because its hydrogenated C9 backbone balances aliphatic compatibility with a softening point high enough to resist blocking during film storage.
| Comparative parameter | NOVARES PURE 1120 class | Conventional non-hydrogenated C9 | C5/C9 copolymer |
|---|---|---|---|
| Nominal softening point | 110–115 °C (ASTM E28) | 90–120 °C | 85–110 °C |
| Molten Gardner colour | ≤1 (ASTM D1544) | 5–10 | 2–4 |
| Acid number | ≤0.1 mg KOH/g (ASTM D974) | ≤0.5 mg KOH/g | ≤0.2 mg KOH/g |
| Volatile content | ≤0.5% (ASTM D2369) | 1.0–3.0% | ≤0.8% |
| Residual aromaticity | Low after hydrogenation | High | Moderate |
| Primary film-processing effect | Reduced melt viscosity, low colour, low odour | High compatibility but strong colour and odour tendency | Intermediate tack and compatibility |
The specification distinction has practical consequences in BOPP film. Non-hydrogenated C9 resins can generate colour bodies during line stops because of retained unsaturation at 250–280 °C; hydrogenated C9 resins are more resistant to this thermal degradation pathway. C5/C9 copolymers may reduce optical haze less predictably because their intermediate aromatic content promotes phase separation at high addition levels in PP-rich layers. NOVARES PURE 1120 is therefore selected where the converter requires a modifier that behaves as a low-viscosity PP-compatible component without introducing a yellow tint or aromatic odour.
Incoming quality control for BOPP film-grade use is structured around the physical and chemical parameters that control melt stability, colour, and volatile contribution. The certificate of analysis typically includes softening point, molten Gardner colour, acid number, ash content, and volatile matter. The table below summarises the technical class ranges commonly referenced for hydrogenated C9 resins of this type; the product data sheet and certificate of analysis for the specific batch take precedence.
| Test parameter | Method | Typical target |
|---|---|---|
| Softening point, ring and ball | ASTM E28 | 110–115 °C |
| Colour, molten Gardner | ASTM D1544 | ≤1 |
| Acid number | ASTM D974 | ≤0.1 mg KOH/g |
| Ash content | ASTM D5630 | ≤0.01% |
| Volatile matter | ASTM D2369 | ≤0.5% |
| Melt viscosity at 180 °C, Brookfield | ASTM D3236 | 300–800 mPa·s |
| Molecular weight, Mw | GPC with polystyrene calibration | 900–1,500 g/mol |
For BOPP film production, the resin is normally introduced as a gravimetrically dosed component in the PP-rich core layer or in a skin-layer masterbatch. The pastille form permits direct dosing into the extruder feed throat, while flake material may require pre-blending with PP granules to avoid segregation. Storage should avoid prolonged exposure to direct sunlight and should maintain a dry, cool environment below 35 °C. Although hydrogenated hydrocarbon resins are not strongly hygroscopic, condensation on cold pastilles can introduce water into the extrusion system; therefore sealed silos or intermediate bulk containers with nitrogen blanketing are used on some film lines to reduce moisture uptake and oxidative surface ageing.
On a sequential tenter-frame BOPP line, NOVARES PURE 1120 is added to the core-layer extruder or to a separate side-stream blending unit before the coathanger die. The resin lowers the melt viscosity of the PP compound, permitting a reduction in melt temperature or an increase in line speed without exceeding the pressure limits of the extruder drive. In actual film-line practice, the processing window is constrained by melt temperature and residence time rather than by the resin alone. Melt temperatures in the range of 230–280 °C are typical for PP film extrusion; residence times above 8 minutes at the upper end of this range should be avoided because thermal oxidative breakdown of the resin can increase volatiles and alter colour. The hydrogenated structure provides a wider thermal stability margin than conventional C9 resins, but it is not an oxidation-proof material. Nitrogen blanketing of the feed hopper and clean-up of any dead zones in the die or screen changer are recommended to prevent yellowing during prolonged extrusion campaigns.
After machine-direction and transverse-direction orientation, the modified PP film may be corona-treated to raise wetting tension for ink, adhesive, or metallisation compatibility. Addition of the resin can shift the surface energy development, so the corona discharge intensity must be re-established for each formulation. Wetting tension is normally checked according to ASTM D2578, with target values often in the range of 38–42 mN/m for printing and laminating applications. Haze and light transmission are measured according to ASTM D1003, while tensile properties are evaluated according to ASTM D882. Published data for the exact effect of NOVARES PURE 1120 on BOPP haze and tensile modulus at every addition level is limited; converters should generate a design-of-experiments matrix on their own film line to establish the relationship between resin loading, stretch ratio, and final film properties.
Reporting of batch-to-batch variation from manufacturing lines indicates that the most common failure modes associated with hydrocarbon resin modification are not from the resin itself but from insufficient mixing in the extruder, incorrect gravimetric dosing calibration, or re-crystallisation of the resin in cold feed zones. Therefore the resin should be fully melted before the high-shear mixing section of the screw, and the feed throat temperature should remain below the softening point to avoid premature sticking. Incompatibilities are limited: the resin should not be combined with strongly acidic or oxidising additive packages, and storage with open exposure to atmospheric oxygen at elevated temperatures should be avoided. Regulatory acceptability for food-contact BOPP films must be verified against the supplier documentation and the applicable compliance framework, such as FDA 21 CFR sections for polyolefin food-contact films or EU 10/2011 migration limits for plastic materials and articles intended to come into contact with food. Where the final film is intended for low-odour or low-taste critical packaging, organoleptic evaluation according to internal converter standards should be performed on the finished rollstock, because residual trace volatiles can be influenced by line temperature profile, vacuum venting efficiency, and corona treatment intensity.