| HS Code | 894511 |
| Product Name | NOVARES TK100 Aliphatic-Modified C9 Resin for Hot-Melt Adhesives |
| Softening Point Ring And Ball | 100 °C |
| Melt Viscosity At 160c | 400 mPa·s |
| Acid Value | 0.5 mg KOH/g |
| Iodine Value | 130 g I2/100 g |
| Glass Transition Temperature | 48 °C |
| Density At 20c | 1.07 g/cm³ |
| Flash Point | 260 °C |
As an accredited NOVARES TK100 Aliphatic-Modified C9 Resin for Hot-Melt Adhesives factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied as pastilles in 25 kg heat-sealed paper bags, palletized and stretch-wrapped for safe storage and transport. |
| Container Loading (20′ FCL) | 20′ FCL container loading of NOVARES TK100 resin: palletized bags, securely packed, ventilated, dry, protected from heat and damage. |
| Shipping | NOVARES TK100 is shipped as solid pastilles in 25 kg multi-wall paper bags or original packaging. Store cool, dry, away from heat, ignition sources, and direct sunlight. Ensure pallets are stable and covered; avoid puncturing bags. Transport by covered truck or container to prevent moisture contamination. Non-DOT regulated. |
| Storage | Store NOVARES TK100 in its original, unopened packaging in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers tightly sealed to prevent contamination and moisture pickup. Avoid prolonged exposure to temperatures above 30°C. Under these conditions, shelf life is typically two years from manufacture. |
| Shelf Life | Shelf life is typically two years from manufacture when stored unopened in a cool, dry place. |
On high-speed corrugated case and carton sealing lines running EVA-based hot melts above 160 °C, the tackifier selection controls melt viscosity, substrate wetting, open time, and cold-storage fiber tear. NOVARES TK100, an aliphatic-modified C9 hydrocarbon resin with a nominal softening point near 100 °C under ASTM E28, is compounded at 25–40 wt% in EVA formulations containing 28–33 wt% vinyl acetate and a melt index of 400–800 g/10 min measured at 190 °C with a 2.16 kg load under ASTM D1238. The aliphatic modification lowers the concentration of reactive aromatic olefin species relative to standard C9 resin, which improves Gardner color retention under ASTM D1544 during extended residence in heated melt tanks. On production lines using 10–20 kg reservoir tanks, piston pump delivery, and heated transfer hoses held at 165–175 °C, the main instability risks are oxygen ingress at the tank surface, skinning, and char accumulation on tank walls. Nitrogen blanketing at 0.1–0.2 bar overpressure and limiting excursions above 180 °C to cleaning cycles of less than 30 min suppress most oxidative viscosity drift. In this application the resin is not a direct food-contact material; compliance for transit packaging is evaluated under FDA 21 CFR 175.105 for indirect contact through the board barrier.
Compression dwell on case erectors running at 35–60 m/min is typically below 1.2 s, so the adhesive must retain pressure-sensitive character until board contact. Increasing TK100 from 25 to 40 wt% shifts the glass transition upward and shortens open time, while reducing tackifier loading and increasing wax fraction can produce brittle cold performance. Production calibration is commonly performed with a kraft-to-kraft loop tack method derived from ASTM D6195 and with fiber tear evaluation after conditioning at −5 °C for 24 h. A useful operational window is 30–35 wt% TK100 combined with a microcrystalline wax having a congealing point of 72–78 °C and an antioxidant package at 0.5–1.0 wt%. This range maintains Brookfield viscosity under ASTM D3236 at 180 °C within the capability of gear pumps sized below 1.5 cm³/rev and nozzle orifice diameters of 0.4–0.6 mm. At loadings above 35 wt%, startup cavitation becomes a documented failure mode on unheated lines, particularly when ambient temperature falls below 10 °C.
Batch-to-batch variability is reduced by pre-blending TK100 with the wax at 130–140 °C before adding EVA, because direct addition of resin granules into molten EVA can create localized overheating and gel particles that block nozzle screens of 100–150 µm mesh. The lower aromatic unsaturation of TK100 reduces but does not eliminate cyclic aromatic oligomers, so migration risk must be checked against REACH Annex XVII Entry 50 restrictions on polycyclic aromatic hydrocarbons and against regional food packaging recommendations where recycled board is used. The following matrix summarizes the test framework for this application.
| Application parameter | Standard or regulation | Function |
|---|---|---|
| Indirect food-contact adhesive | FDA 21 CFR 175.105 | Permitted components for indirect food contact through a functional barrier |
| Hot-melt viscosity | ASTM D3236 | Brookfield viscosity at 180 °C |
| Resin softening point | ASTM E28 | Ring-and-ball softening point |
| Shear adhesion failure temperature | ASTM D4498 | Heat resistance during warehouse transport |
| Melt index of EVA | ASTM D1238 | Polymer flow specification at 190 °C, 2.16 kg |
| Loop tack | ASTM D6195 | Open-time and pressure-sensitive character |
| Gardner color | ASTM D1544 | Heat-aging color stability |
| PAH restriction | REACH Annex XVII Entry 50 | PAH content limits in supplied material |
During perfect-binding at gathering speeds above 12,000 cycles/h, twin-roller spine applicators and side glue extrusion units deposit EVA hot melt at 150–165 °C onto milled book spines. The adhesive must penetrate paper fibers sufficiently for page pull while retaining enough hinge flexibility to pass layflat and cold crack tests. NOVARES TK100 is compounded at 20–35 wt% with an EVA grade containing 33 wt% vinyl acetate and having a melt index of 400 g/10 min under ASTM D1238. The aliphatic-modified C9 resin increases adhesion to clay-coated and UV-cured cover stocks by moderating interfacial wetting without the strong yellowing produced by conventional aromatic C9 tackifiers. Because the aliphatic modification reduces aromatic unsaturation, adhesive films with hinge thicknesses of 0.3–0.6 mm show lower absorbance change under accelerated UV exposure following ASTM D4329 cycle A, although published numerical data for this specific product configuration is limited. The resin also contributes to maintaining page pull above 7.0 N/cm on uncoated paper at 23 °C when adhesive penetration is adequate.
Cold crack resistance is evaluated by flexing bound book blocks after conditioning at −5 °C for 24 h and by tensile elongation of free films under ASTM D638. A formulation containing 28 wt% TK100, 35 wt% EVA, 25 wt% Fischer-Tropsch wax, and 12 wt% rosin ester balances adhesion and low-temperature stiffness. In side gluing, nozzle temperatures below 150 °C can produce stringing, while temperatures above 175 °C can generate oxidative gel specks that interfere with roller transfer. The aliphatic modification allows application temperature reductions of 5–8 °C relative to an equivalent softening point aromatic C9 tackifier. Oil-jacketed pre-melters without dead zones are preferred over direct electric cartridge heating to limit localized thermal degradation. For books required to withstand hot-cold cycling from −20 °C to 60 °C, TK100 alone is not sufficient; a secondary hydrogenated tackifier or rosin ester is blended to extend the service window.
For nonwoven lamination in hygiene applications, SBC-based adhesives are sprayed through multi-bead or curtain coat heads at line speeds above 300 m/min. NOVARES TK100 functions as a tackifying resin in SIS/SBS systems at total resin loadings of 45–60 wt%. The aliphatic-modified C9 structure permits partial replacement of fully aliphatic C5 resin to improve cohesive strength while maintaining low color. At application temperatures of 150–160 °C, the complex viscosity measured by oscillatory rheometry under ISO 6721-10 must remain below the shear-stability limit of the application head. The cooling spray must also retain a low elastic modulus so that polypropylene nonwoven fibers do not break during laminate consolidation. In spiral spray application, process air at 0.5–1.5 bar and nozzle-to-substrate distances of 15–30 mm produce adhesive filament diameters of 50–150 µm.
Adding TK100 at 15–25 wt% to an SIS/oil compound raises the glass transition relative to the oil-extended polymer alone, improving shear holding power as assessed by a modified ASTM D4498 method. Loadings above 30 wt% can reduce low-temperature peel on polyethylene film below 1.5–2.5 N/cm at 5 °C. The critical process conflict is fogging and odor; the resin must have a volatile fraction below the supplier specification limit and no visible smoke at application temperature. Published data for this specific configuration is limited, so production trials should include thermogravimetric analysis at 150 °C for 2 h to quantify mass loss before line qualification. The use of TK100 in elastic strand attachment for leg cuffs requires creep resistance at 38 °C, but the formulation must keep Brookfield viscosity at 150 °C below 5,000 mPa·s for fine spiral patterns.
Equipment with gear pumps of 1.2 cm³/rev displacement and heated hoses shorter than 5 m tolerates higher resin levels than systems with long heated hoses and stagnant zones. Incompatibility may arise with high-diblock SIS grades, where the aromatic-rich domains in TK100 produce a translucent melt but a cloudy solid, indicating limited miscibility. A film clarity check after 24 h at 23 °C using ASTM D1003 on a 0.5 mm pressed film can identify haze above 10 %, which indicates a need for lower TK100 loading or a higher aliphatic content. This haze is a practical operational limit for visible nonwoven materials, but it is less relevant for heavily pigmented laminates.
At the panel edge, edge banding lines for furniture present a high-temperature short-open-time application in which the hot melt is applied to a 0.4–2.0 mm PVC, ABS, or PET edge strip and immediately pressed onto a melamine-faced board. EVA-based edge banding adhesives with 10–20 wt% calcium carbonate filler are processed at 190–210 °C in heated roller reservoirs. NOVARES TK100 at 15–25 wt% provides adhesion to polar PVC edge tapes without the darkening associated with unmodified C9 resins during high-temperature processing. Because the melt is exposed to air in open roller systems, thermal stability is the controlling parameter. The aliphatic modification improves Gardner color retention at 200 °C for 4 h compared with standard C9, but it does not confer the stability of fully hydrogenated tackifiers. Formulators often combine TK100 with a small amount of hydrogenated rosin ester to limit surface skinning and char formation in the roller trough.
The process window is defined by the bondline temperature at the pressure roller. Board surface temperatures below 15 °C can freeze the adhesive before wetting and cause visible edge lift, while melt temperatures above 220 °C increase volatile loss, odor, and black speck contamination. Screw pumps delivering to a slot nozzle with a width of 0.3–0.5 mm require a Brookfield viscosity at 200 °C low enough to avoid overpressure. Filler content should remain below 20 wt% because high filler raises low-shear viscosity and reduces wetting on melamine surfaces. Adhesion is tested by a 90° peel method derived from ASTM D1876 after 24 h conditioning; the practical target is cohesive failure within the adhesive rather than adhesive failure from the edge tape. Moisture in the board or edge strip can cause bubble defects when the melt temperature exceeds the boiling point of entrapped water, and calibrated infrared preheating of the panel edge to 35–50 °C reduces this failure mode. TK100 is not recommended as the sole tackifier in high-temperature edge banding grades where melt color must remain below Gardner 3 after 8 h at 200 °C; in such systems it is partially replaced by hydrogenated C9 or aliphatic resin.
When APAO-based hot melt adhesives are applied to untreated polypropylene and ABS, the long open time and low surface energy of the substrates require a tackifier that does not excessively raise the glass transition or destroy flexibility. NOVARES TK100 is introduced at 10–20 wt% to modify open time and cohesive strength while maintaining the inherently long bonding range of APAO. The aliphatic-modified C9 resin has partial compatibility with APAO; at loadings above 25 wt%, cloud point and phase separation can occur in low-ethylene APAO grades, reducing peel performance. Because APAO melts are typically applied at 150–170 °C, the aromatic character of TK100 contributes to heat resistance as measured by ASTM D4498, but it may also increase low-temperature brittleness. A general target formulation includes 50–70 wt% APAO, 10–20 wt% TK100, 10–20 wt% aliphatic resin, and 10–15 wt% polypropylene wax.
On assembly lines with robot-mounted hot melt nozzles and automatic part feeding, the adhesive is exposed to variable open times from 3 to 20 s. The TK100 content is adjusted according to the cool-down rate of the bondline; thicker substrates with higher heat capacity require lower resin levels to avoid premature set. Adhesion to untreated polypropylene is evaluated by lap shear in accordance with ISO 4587 after 24 h at 23 °C and 50 % RH. Because the surface energy of untreated PP is typically 29–31 mN/m, mechanical interlocking and viscoelastic energy dissipation dominate the bond. The higher modulus imparted by TK100 can reduce the ability to absorb peel stress, so for vibration-prone assemblies the loading should remain at the low end of the stated range. For small appliance assembly where heat resistance above 60 °C is not required, conventional APAO formulations may not need TK100. Its use in this segment is limited to specific color-sensitive white or light-colored assemblies where unmodified C9 resin would cause unacceptable yellowness under warehouse skylight exposure. Published data for this specific configuration is limited, making pilot-line compatibility testing necessary before full qualification.
Because hot-melt pressure-sensitive adhesives for label stock require a balance of tack and shear, the tackifier system must shift the rubbery plateau modulus without producing excessive melt viscosity. NOVARES TK100 at 30–45 wt% on total formulation serves as a mid-block and endblock compatible tackifier in SIS or SBS systems, increasing storage modulus and the glass transition of the rubbery phase. The aliphatic modification reduces yellowing compared with standard C9 tackifiers, which is relevant for white and pigmented label facestocks. Slot-die coating lines operating at 140–160 °C require a Brookfield viscosity below 7,000 mPa·s at the coating head. If TK100 loading exceeds 45 wt%, the viscosity can exceed the capacity of 2 cm³/rev gear pumps, and the adhesive may lose tack because the glass transition moves too close to room temperature.
Loop tack is measured according to ASTM D6195, 180° peel according to ASTM D3330, and shear holding power according to ASTM D3654. A typical SIS/TK100 system performs acceptably at adhesive coat weights of 18–25 g/m², provided endblock styrene domains remain intact at 23 °C. The aliphatic-modified C9 resin is not a direct substitute for fully aliphatic C5 resin in clear labels because its remaining aromatic content can raise color and reduce UV stability. For clear film facestocks, TK100 is often blended at only 10–20 wt% with a fully aliphatic resin to control haze. The principal limitation is compatibility with low-styrene diblock-rich SIS grades; high diblock content combined with TK100 may produce a soft adhesive with low shear holding power and edge ooze. Published data for high-temperature shear stability in this specific configuration is limited, so shear holding power at 40 °C should be verified under ASTM D3654 before specifying the resin for aggressive label applications.
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NOVARES TK100 is supplied as an aliphatic-modified C9 aromatic hydrocarbon resin intended for tackification in hot-melt adhesives. The grade designation corresponds to a nominal ring-and-ball softening point of 100 °C, with commercial materials in this class commonly certified to ASTM E28 and reported within a ±5 °C tolerance band. In EVA-based hot-melt compounding, it is added at 20–45 wt% alongside 25–40 wt% EVA copolymer, 15–35 wt% paraffin or Fischer–Tropsch wax, and 0.5–1.5 wt% stabilizer. The aliphatic modification lowers aromatic density relative to a straight C9 stream while retaining sufficient aromatic character for cohesive strength. Published data for NOVARES TK100 as a discrete grade is limited; therefore, the numerical ranges below should be confirmed against a current certificate of analysis. Typical lot-to-lot variation for this class includes Gardner colour in the range 4–7 under ASTM D1544, acid number below 0.5 mg KOH/g under ASTM D974, and melt viscosity from 0.6–1.5 Pa·s at 200 °C under ASTM D3236. Gel-permeation chromatography against polystyrene standards generally shows weight-average molecular weight between 800–2,500 g/mol and polydispersity near 2.0–2.8. The resin is hydrophobic and normally supplied as flakes or pastilles; bulk density depends on flake geometry and can be lower than the true density of approximately 1.00–1.05 g/cm³.
The aliphatic modification shifts solubility parameter from roughly 9.0 (cal/cm³)0.5 for a standard aromatic C9 stream to approximately 8.5–8.8 (cal/cm³)0.5. This positions the resin closer to the aliphatic-rich segments of EVA and the rubbery midblock of SIS/SBS block copolymers. The practical result is a lower cloud point in molten EVA and reduced phase separation after cooling. The resin retains sufficient aromatic character to contribute heat resistance and cohesive strength; this distinguishes it from pure C5 aliphatic tackifiers, which give rapid wetting and low-temperature tack but often soften below 80 °C and produce lower shear resistance. Compared with unmodified C9 resin of the same nominal softening point, the aliphatic-modified grade reduces aromatic odour, improves compatibility with low-density polyethylene, and lowers colour development during heated storage. Compared with hydrogenated C9 or hydrogenated hydrocarbon resins, NOVARES TK100 retains more aromatic unsaturation and therefore shows lower UV stability and higher yellowness under accelerated weathering, but it does not require hydrogenation-related catalyst removal and typically presents a lower raw-material cost. In applications where high shear adhesion is required on polar substrates, the aromatic retention is an advantage; in applications requiring water-white colour after prolonged UV exposure, a hydrogenated resin is usually preferred.
In molten adhesive formulation, the compatibility change is observed as a reduction in phase-separation haze and better wetting on untreated polyethylene and corona-treated polypropylene. The resin should not be considered a direct replacement for all unmodified C9 grades, because the aliphatic fraction can reduce specific adhesion to metals, glass, and aluminium in some assembly applications. Grade-specific peel and lap-shear data for NOVARES TK100 are limited; therefore, substitution trials should compare heat-fail temperature and substrate failure mode under the end-use condition rather than relying solely on softening point equivalence.
On production-scale corotating twin-screw extruders with 32:1 to 44:1 L/D ratios, the resin is metered into the feed throat or side feeder after the polymer has formed a melt seal. Feed-zone set points are typically 110–130 °C, mid-barrel zones 150–170 °C, and die temperature 175–180 °C. At throughputs of 200–300 kg/h, residence time is held under 20 min to limit thermal history. During line stoppages, material held at 170 °C for more than 60 min can form surface skin at the die lip; operators typically purge with low-viscosity wax before restart to clear nozzle deposits. The aliphatic-modified grade is reported to generate less dark oxidation product than standard C9 resin under stale-material conditions, but the improvement is less pronounced than that of hydrogenated tackifiers. Single-screw extruders with low L/D below 20:1 are not recommended for high-tackifier formulations because dispersion uniformity of resin and wax becomes dependent on back pressure. This creates local viscosity heterogeneities and increases the risk of charring on screw flights.
Batch mixing remains common in smaller hot-melt operations. Anchor-agitated mixers operated at 160–170 °C can produce acceptable adhesive when throughput is below 500 kg/h, but shear history is less consistent than in twin-screw lines. In batch practice, lot-to-lot colour stability is more sensitive to hold time and exposed surface area. Nitrogen blanketing reduces oxidative film formation, and phenolic-phosphite stabilizer packages are used to suppress viscosity drift. The resin’s low acid number of 0.5 mg KOH/g or below limits acid-catalyzed rearrangement, but the material should not be held above 200 °C for residence times beyond 2 h without documented melt-stability testing.
At 180 °C, hot melts containing 20–45 wt% of a 100 °C aliphatic-modified C9 tackifier and EVA with 28% vinyl acetate typically exhibit Brookfield viscosities of 800–1,500 mPa·s under ASTM D3236. The melt is shear-thinning under high-shear slot-die application; viscosity at 1,000 s⁻¹ can be one-half to one-third of the low-shear value. This is important for gear-pump delivery because low-shear viscosity alone under-represents pressure drop across the die. During extended campaigns, oxidative chain extension can increase low-shear viscosity by 20–40% after 4 h at 190 °C in vented mixers unless the melt is blanketed with nitrogen and stabilized. The aliphatic modification slows colour-body formation relative to unmodified C9 but does not confer oxidative stability comparable with hydrogenated tackifiers. For automatic coating lines with slot dies, filtration through 80–120 mesh screens is common to capture char particles and incidental gels. Pressure rise across screen packs is a practical indicator of resin thermal stability; a rapid increase with time is often caused by stale material in dead zones rather than by the virgin resin itself.
Table 1 compares class-level selection factors for unmodified C9, aliphatic-modified C9, and hydrogenated hydrocarbon tackifiers in EVA and SBC hot-melt systems. The values are indicative of typical supplier technical literature and are not grade-specific certification limits for NOVARES TK100.
| Selection factor | Unmodified C9 resin | Aliphatic-modified C9 resin | Hydrogenated hydrocarbon resin |
|---|---|---|---|
| Gardner colour | 7–12 | 4–7 | <1 |
| Softening point | 95–105 °C | 95–105 °C | 95–105 °C |
| Melt viscosity at 200 °C | 0.5–1.5 Pa·s | 0.6–1.5 Pa·s | 1.0–3.0 Pa·s |
| UV and thermal stability | Low | Moderate | High |
| Aromatic odour | Strong | Reduced | Low |
| Compatibility with LDPE | Limited | Improved | High |
| Relative cost index | 1.0 | 1.1–1.3 | 2.5–4.0 |
For packaging adhesives applied to corona-treated LDPE and clay-coated carton stock at line speeds up to 120 m/min, the tackifier level is typically maintained at 35–45 wt% to keep open time between 10–20 s measured by ASTM D4498. At −18 °C, fibre tear on corrugated stock is controlled mainly by EVA vinyl acetate content and wax melting point; the aliphatic modification contributes by lowering the glass transition of the tackifier-rich phase and reducing brittle failure. In comparison, an unmodified C9 resin of equal softening point can give higher room-temperature cohesive strength but increases brittle failure at low temperature and may require higher plasticization to maintain wetting on LDPE. A pure C5 resin improves cold wetting but reduces heat resistance; for adhesives requiring peel-fail temperatures above 65 °C, the retained C9 fraction in an aliphatic-modified grade is beneficial.
Differences from other products are also observed in product assembly applications. In manual-gun and roll-coater operations with open assembly times of 15–30 s, the resin’s moderate polarity supports adhesion to ABS, wood, and polyester foil, while its aliphatic character reduces stringing compared with high-aromatic C9 grades. On aluminium and galvanized steel, cohesive strength may be lower than with a high-aromatic resin because the aliphatic modifier reduces specific acid-base interaction at the metal oxide surface. For structural hot melts requiring high load-bearing resistance, a pure aromatic C9 or a rosin ester may be preferable after compatibility testing.
Regulatory and compatibility boundaries should be confirmed before use. The resin is hydrophobic and does not require pre-drying in closed bulk handling; however, condensate entering a hot-melt mixer can create localized steam and viscosity valleys. For indirect food packaging adhesives, compliance with 21 CFR 175.105 must be verified against the specific formulation and the supplier’s current regulatory statement. Similarly, REACH registration under Regulation EC 1907/2006 and heavy-metal screening under RoHS Directive 2011/65/EU annex II are typically covered by the producer’s safety data sheet, but batch-level verification is recommended when importing into jurisdictions with updated restrictions. The resin should not be combined with strong protic acids or amine-functional additives without testing, because the aromatic fraction can undergo acid-catalyzed rearrangement and amine-induced chromophore formation. Grade-specific extraction data for NOVARES TK100 under food-contact simulating conditions is limited; therefore, a written compliance statement from the producer is required before use in sensitive applications.