| HS Code | 719157 |
| Chemical Family | Hydrocarbon resin |
| Appearance | Clear viscous liquid |
| Color Gardner | 2 max |
| Viscosity At 25 C Brookfield Cp | 20000-50000 |
| Specific Gravity At 25 C | 0.92-0.95 |
| Softening Point | Liquid at room temperature |
| Flash Point C Coc | >200 |
| Acid Value Mg Koh G | <1 |
| Iodine Value | 20-40 |
| Glass Transition Temperature C | -20 to -10 |
| Number Average Molecular Weight Mn | 300-500 |
| Solubility | Soluble in aliphatic, aromatic, and cycloaliphatic hydrocarbons; insoluble in water |
As an accredited Liquid Eastman 1020 Hydrocarbon Resin for Tackifier & PSA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Liquid Eastman 1020 Hydrocarbon Resin supplied in 200 kg steel drums for tackifier and pressure-sensitive adhesive applications. |
| Container Loading (20′ FCL) | 20′ FCL: Liquid Eastman 1020 hydrocarbon resin loaded in drums/IBCs, secured and blocked for safe transit, for tackifier/PSA use. |
| Shipping | Liquid Eastman 1020 ships in heated or insulated tanks, isotanks, or drums to maintain viscosity. Use dedicated equipment to prevent contamination. Handle as a combustible material; ground containers, avoid static ignition. Ensure spill containment and follow local regulations for hydrocarbon transport. Provide ventilation and personal protective gear during transfer. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, and open flames. Keep container tightly closed when not in use to prevent contamination or moisture pickup. Avoid contact with strong oxidizers and incompatible materials. Maintain temperatures within recommended range to preserve viscosity and performance, ensuring safe handling and product integrity. |
| Shelf Life | Shelf life is typically two years from manufacture when stored in original sealed containers at moderate temperatures. |
Polyolefin label facestock with a corona-treated surface is coated with a 100% solids hot-melt pressure-sensitive adhesive in which liquid Eastman 1020 hydrocarbon resin is used at addition levels between 42 wt% and 58 wt% in a styrene-isoprene-styrene (SIS) triblock matrix. The mixer is a jacketed sigma-blade kneader with usable capacity of 500 L and counter-rotating blade speed of 30 rpm. Nitrogen blanketing at 2 kPa positive pressure limits thermo-oxidative colour rise. The block copolymer is masticated at 150 °C for 20 min before the resin is metered over 30 min through a heated gear pump. The finished batch is held at 140 °C for 15 min under vacuum of -0.08 MPa to remove entrained air. Viscosity is measured per ASTM D3236-88 with a Brookfield RVT Thermosel, spindle 27, at 10 rpm and 140 °C. The target viscosity window for slot-die and rotary screen application is 4,000–12,000 mPa·s. Batches outside this band are adjusted with 1–2 wt% increments of the liquid resin rather than process oil to preserve shear adhesion failure temperature. Final coat weight on siliconized PET liner is verified on-line by beta gauge at 20 ± 1.5 g/m².
Compliance for direct food-packaging label stock is assessed under FDA 21 CFR 175.125 for pressure-sensitive adhesives used in food-contact articles and under FDA 21 CFR 175.105 for general adhesives where a functional barrier separates the adhesive from food. The finished construction is tested using distilled water, 10% ethanol, and 3% acetic acid food simulants under conditions of 40 °C for 10 days followed by room temperature for 10 days. Peel adhesion is recorded per ASTM D3330/D3330M-04 Test Method A on stainless steel after 24 h dwell. Loop tack is recorded per ASTM D6195-03. Holding power is measured per ASTM D3654/D3654M-06 at 1 kg load on a 25 mm by 25 mm bonded area. Industrial specifications commonly require 180° peel values between 14 N/25 mm and 22 N/25 mm on stainless steel, loop tack above 12 N/25 mm, and static shear at 23 °C above 4 h. Batch-to-batch viscosity variation at 140 °C is held within ±10% of the reference lot to prevent coat weight shifts on slot-die coating stations.
Process records from production-scale SIS compounding lines indicate that at resin fractions above 62 wt%, loop tack under ASTM D6195-03 decreases by more than 20% relative to a 55 wt% loading because the liquid resin begins to plasticize the polystyrene endblock domains. This is detected as a reduction in storage modulus G′ at 25 °C from a plateau of 0.8 MPa to below 0.3 MPa at 1 Hz on an 8 mm parallel-plate dynamic mechanical analyser operated per ISO 6721-1:2019. Static shear under ASTM D3654/D3654M-06 at 1 kg load declines from 4.2 h to 0.9 h when resin loading exceeds 62 wt%. The upper loading boundary is therefore maintained at 60 wt% unless an endblock-compatible C9 resin at 3–5 wt% is added. Pre-drying of the block copolymer at 60 °C for 2 h is required when ambient relative humidity exceeds 60%, because free moisture raises batch viscosity unevenly and creates microvoided adhesive film after vacuum stripping. The liquid resin is transferred through heated lines at 130 °C; dead zones in unheated pipe below 110 °C cause intermittent solidification and should be eliminated with hot-oil jacketing.
Multiline construction bonding for disposable hygiene uses an amorphous poly-alpha-olefin (APAO) hot-melt adhesive in which liquid Eastman 1020 hydrocarbon resin is added at 8–15 wt% alongside 5 wt% Fischer-Tropsch wax. The adhesive is dispensed through heated hoses and an application head with air-assisted spiral spray nozzles at 130–145 °C. Brookfield viscosity at 135 °C is measured per ASTM D3236-88 with spindle 27 at 5 rpm and is maintained between 2,000 mPa·s and 3,800 mPa·s. Spray pattern stability is checked on a 45 cm by 45 cm polypropylene nonwoven target moving at 300 m/min. A single-spiral width deviation beyond ±2 mm triggers nozzle temperature adjustment of 2 °C increments, not resin loading changes. Open time is 4–6 s as determined by an automated fibre-tear probe on 15 g/m² spunbond nonwoven at 23 °C and 50% RH. Compression is applied within 1.5 s after deposition at 0.2 MPa for 0.8 s.
Below 8 wt% resin, the adhesive loses cohesive fibre tear on polypropylene nonwovens after 24 h at 40 °C and 80% RH. Above 15 wt%, the spiral pattern becomes discontinuous because extensional viscosity at the nozzle exit falls below the level required for filament formation. The failure mode is recorded on pilot lines with a six-port metering pump and 0.028 inch nozzle orifices. Start-up viscosity overshoot is limited to less than 10% of set point by staged hot-oil heater zones and a 5 min recirculation cycle before dispensing. Final nonwoven T-peel is measured per ASTM D1876 at 25 mm/min and remains between 1.8 N/25 mm and 3.0 N/25 mm after three weeks at 50 °C. Compliance screening follows European Regulation EC No 1907/2006 for REACH candidate list content below 0.1% w/w per article component. The adhesive is not formulated for food-contact but is screened against brand-level volatile organic compound limits using static headspace GC/MS at 150 °C for 30 min.
Corrugated case and carton sealing lines using high-pressure piston pumps and slot-coat nozzles require a low-viscosity EVA hot-melt adhesive. Liquid Eastman 1020 hydrocarbon resin is applied at 15–25 wt% in an ethylene-vinyl acetate copolymer with 28% vinyl acetate content and 20 wt% microcrystalline wax. Viscosity at 150 °C is measured per ASTM D3236-88 with spindle 27 at 20 rpm and is held below 800 mPa·s. Higher viscosity at this temperature causes stringing and poor tail cut-off on packaging lines above 60 cases/min. Open time is measured with a bench-top compression tester on clay-coated board at 23 °C and 50% RH, with bonding pressure of 0.3 MPa for 2 s. The target open time is 3–5 s, allowing flap compression before fibre-tearing adhesion develops.
Adhesive that remains above 25 wt% resin exhibits a drop in heat resistance measured by a shear adhesion failure temperature test per ASTM D4498-07 from 78 °C to below 68 °C, risking carton pop-open during summer truck transport. The EVA grade also has a narrow melting window. Barrel zones on the melter should be set at 140 °C, 150 °C, and 155 °C, and the adhesive should not be held above 160 °C for more than 4 h. Food-contact status is evaluated under FDA 21 CFR 175.105, with total non-volatile extractives in n-heptane and 95% ethanol below the applicable migration thresholds specified in the regulation. RoHS Directive 2011/65/EU Annex II restrictions for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE are met by the resin and the compounded adhesive with each restricted substance below 1,000 ppm or 100 ppm as applicable by homogeneous material weight.
Low-bleed bookbinding and case-making adhesives formulated with ethylene-vinyl acetate copolymers of 18–25% vinyl acetate content require a tackifier that does not crystallise under room-temperature flexing of the spine. Liquid Eastman 1020 hydrocarbon resin is metered into a twin-screw extruder with L/D 40:1 at 12–20 wt%. Barrel temperatures are set from 120 °C at the feed throat to 150 °C at the die. The extrudate is pelletised and then re-melted in a melter for spine glue application. T-peel of paper-to-paper bonds is measured per ASTM D1876 at 25 mm/min and shall exceed 2.2 N/mm for 400-page sewn book blocks. Cold crack resistance is evaluated at -20 °C by flexing a 2 mm adhesive film over a 12 mm mandrel in accordance with ASTM D522/D522M-13, with no visible cracking after a 180° bend. Accelerated ageing for 14 days at 60 °C is used to measure oil migration into uncoated paper; staining beyond 1 mm from the adhesive line is cause for rejection. The adhesive is screened under European REACH Article 33 for SVHC below 0.1% w/w and under California Proposition 65 for listed solvents. Finished bookblock adhesive has total volatiles below 2% as measured by thermogravimetric analysis at 160 °C for 30 min.
| Application segment | Primary standard or regulation | Typical control specification |
| Food-label SIS HMPSA | FDA 21 CFR 175.125; ASTM D3330/D3330M-04 | Peel 14–22 N/25 mm on stainless steel; static shear above 4 h |
| Hygiene APAO construction | ASTM D1876; REACH EC No 1907/2006 | T-peel 1.8–3.0 N/25 mm after 3 weeks at 50 °C |
| Corrugated case sealing EVA | FDA 21 CFR 175.105; ASTM D4498-07 | SAFT ≥ 68 °C; melt viscosity below 800 mPa·s at 150 °C |
| Bookbinding EVA | ASTM D1876; ASTM D522/D522M-13 | Paper-to-paper T-peel above 2.2 N/mm; no cracking at -20 °C |
| Solvent-borne masking tape | ASTM D3330/D3330M-04 | Dry peel 3.8–5.5 N/25 mm on stainless steel |
| Butyl sealant | ASTM D1646; ASTM E2190 | ML(1+4) at 100 °C: 35–45 MU; water absorption ≤ 0.15% after 2,160 h |
Masking tape for automotive refinish and general surface protection is coated from a 55% solids natural rubber solution in which liquid Eastman 1020 hydrocarbon resin is used at 50–70 phr on rubber solids. The coating solution viscosity is measured by Ford cup No. 4 at 25 °C and is maintained between 60 s and 90 s. Coagulation or resin drop-out is monitored by a 100 µm filter pressure rise below 0.1 MPa over an 8 h production shift. Adhesive is applied by reverse roll coater to creped paper at 60–80 g/m² wet coat weight and dried in a multi-zone oven with air temperatures from 70 °C to 110 °C and residence time of 90 s. Dry film peel on stainless steel per ASTM D3330/D3330M-04 Test Method A is between 3.8 N/25 mm and 5.5 N/25 mm. Wet-out on plate glass is inspected visually under cross-polarised light to identify gel particles larger than 0.2 mm. Tape that is dried below 1% residual solvent shows acceptable unwind and no adhesive transfer after 72 h at 50 °C on a painted panel. Above 75 phr resin, the dried film loses cohesive strength and transfers adhesive residue to the substrate. The solvent system is typically toluene/n-hexane; therefore the coating line must be explosion-proof and comply with local VOC emission limits under Directive 2004/42/EC where applicable for industrial adhesives. Published data for the specific solvent retention of this resin in natural rubber is limited; full-scale drying trials are required for any new oven profile.
Butyl sealant for insulated glass units and metal-to-glass sealing uses a butyl rubber/polyisobutylene matrix in which liquid Eastman 1020 hydrocarbon resin is compounded at 10–18 wt% with carbon black and ground calcium carbonate. Mixing is performed in a vacuum sigma-blade kneader at 110 °C for 60 min under -0.09 MPa. Compound viscosity is measured per ASTM D1646 as Mooney ML(1+4) at 100 °C, target 35–45 MU. Tack compounds are aged in distilled water at 23 °C for 2,160 h; water absorption shall not exceed 0.15% by mass. Residual tack is tested by a probe-tack apparatus at 23 °C with a stainless steel probe of 6 mm diameter and separation speed 50 mm/min. The tack force after ageing shall remain above 80% of the unaged value. Formulations above 18 wt% resin have a 90-day water-absorption value above 0.15%, causing fogging on the inner glass surface during accelerated weathering. The formulation should not be combined with amine-based adhesion promoters that induce premature crosslinking in halogenated butyl systems. Finished sealant is evaluated under ASTM E2190 for insulating glass edge seal durability; published data for this specific resin in full IG units is limited, so qualification must be performed on production line geometry rather than laboratory coupons.
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Liquid Eastman 1020 Hydrocarbon Resin is supplied as a low-molecular-weight aliphatic C5 tackifying resin with pourable behavior at 25°C. The grade is intended for hot-melt and solvent-borne pressure-sensitive adhesive formulations based on styrene-isoprene-styrene, styrene-butadiene-styrene, natural rubber, and selected acrylic systems. Published typical properties from supplier technical literature include a ring-and-ball softening point below 25°C by ASTM E28, a Gardner color of ≤1.5 by ASTM D1544, a Brookfield viscosity at 25°C of 500–2,000 mPa·s by ASTM D2196, and a closed-cup flash point above 150°C by ASTM D93. These values are class-consistent release ranges, not lot-specific acceptance limits. The product is used primarily as a low-softening-point modifier in high-tack label, film, and nonwoven adhesives, and as a partial replacement for solid hydrocarbon or rosin ester tackifiers to reduce melt viscosity and improve low-temperature wet-out.
Molecular weight data for liquid aliphatic C5 hydrocarbon resins of this type generally place number-average molecular weight Mn in the 400–800 g/mol range and weight-average molecular weight Mw in the 800–2,000 g/mol range by gel permeation chromatography with polystyrene calibration. Because the supplier may not publish GPC data for this specific grade, these values should be treated as class-level ranges rather than lot-specific release data. Viscosity-temperature response is strongly non-Arrhenius near the glass transition; heating from 25°C to 80°C reduces neat resin viscosity by more than one order of magnitude, enabling heated liquid injection without high-pressure piping. The low melt viscosity also supports high-solids solvent-borne coating when the resin is supplied as a 50–70% solids cut in aliphatic or dearomatized hydrocarbon solvent.
In SIS-based hot-melt pressure-sensitive adhesives, the aliphatic resin associates preferentially with the polyisoprene midblock because the Hildebrand solubility parameters of the resin and polyisoprene both fall in the 8.0–8.2 (cal/cm³)0.5 range. This midblock association reduces elastomer plateau modulus, shifts the loss tangent maximum toward lower temperatures, and improves adhesive wet-out at lower lamination or coating pressures. The practical result is an increase in loop tack and 180° peel adhesion on stainless steel under ASTM D3330/D3330M conditions when the liquid resin is incorporated at 10–30 wt% of total adhesive solids. However, the same softening effect reduces shear adhesion failure temperature and static shear resistance. In high-diblock, low-vinyl SIS formulations, loadings above 30 wt% have been associated with cohesive failure and residue on polypropylene label facestocks in 24 h static shear evaluations at 70°C under PSTC-107 or ASTM D3654/D3654M shear conditions. Published data for this specific resin and adhesive configuration is limited; therefore, the cited boundary should be verified through designed experiments using the production SIS grade and coating line.
Rheological screening under parallel-plate oscillation at 1 Hz and 25°C typically shows storage modulus G′ below the Dahlquist tack threshold of 3×10⁵ Pa when Liquid Eastman 1020 is combined with a solid C5 resin at a liquid-to-solid ratio of 1:2 or greater. The exact threshold depends on elastomer molecular weight, diblock content, and endblock styrene fraction. The viscous component G″ increases relative to the elastic component at low frequencies, correlating with pressure-sensitive tack response. Migration of the low-molecular-weight resin to the adhesive-substrate interface can occur after aging at 40°C in nonpolar polyolefin label films; this should be evaluated by surface contact-angle measurement or ATR-FTIR after accelerated aging. For nonwoven elastic-attachment adhesives, the resin is used at the low end of the loading range because higher tackifier content reduces creep resistance under dynamic waistband extension.
For film labels, the liquid resin is blended with a solid C5 tackifier at a liquid-to-solid ratio of 1:3 to 1:1 to balance mandrel hold and peel on polyethylene bottles. In removable labels, the resin is used at restricted levels to avoid adhesion build after aging. In pressure-sensitive tapes based on natural rubber, the resin improves tack but does not replace the need for a zinc oxide or phenolic co-vulcanization system for shear strength. In EVA-based assembly adhesives, Liquid Eastman 1020 can improve open time and low-temperature flexibility, but it should not be used as the sole tackifier when the bonded joint must withstand sustained load above 60°C.
The liquid aliphatic C5 structure distinguishes Liquid Eastman 1020 from solid C5 hydrocarbon resins and from aromatic C9 or dicyclopentadiene tackifiers. The absence of a pastille or flake morphology permits direct metering into the melt zone without pre-grinding, and the low softening point reduces hot-melt processing temperature by lowering the melt viscosity of the fully formulated adhesive. Table 1 provides a comparative direction from typical published data and is not a substitute for formulation-specific testing.
| Tackifier Class | Softening Point (°C) | Typical Color (Gardner) | Compatibility with SIS Midblock | Relative Shear Resistance |
|---|---|---|---|---|
| Liquid Eastman 1020 | below 25 | ≤1.5 | High | Lower |
| Solid C5 hydrocarbon resin | 85–110 | 1–3 | High | Moderate |
| Aromatic C9 hydrocarbon resin | 95–120 | 5–10 | Limited | Higher |
| Rosin ester tackifier | 80–110 | 3–6 | Moderate | Moderate to high |
Compared with a solid C5 resin of similar aliphatic chemistry, Liquid Eastman 1020 reduces hot-melt viscosity but lowers cohesive strength at equal tackifier loading. Compared with aromatic C9 or DCPD resins, the aliphatic C5 grade offers lower Gardner color, improved ultraviolet stability, and lower aromatic content; however, compatibility with polar surfaces is lower, and adhesion to polyethylene terephthalate or metalized film may develop more slowly unless a polar co-tackifier or resin modifier is included. Compared with rosin esters, the hydrocarbon resin has no acid number and does not contribute to ester hydrolysis in humid service, but it provides less specific adhesion to paper and wood fibers. In removable label formulations, a small addition of a polar adhesion promoter may be required when the liquid hydrocarbon resin replaces a rosin ester grade.
Compared with hydrogenated hydrocarbon resins, Liquid Eastman 1020 is not a fully hydrogenated grade. Aliphatic C5 chemistry provides lower initial color and better midblock compatibility than aromatic C9 but retains some unsaturation. In high-temperature nonwoven lines that hold adhesive at 160°C for more than 8 h, oxidative color development can occur unless a hindered phenol or phosphite stabilizer is included. Hydrogenated tackifiers should be selected when extended melt stability and color retention in white or clear label constructions are critical.
In twin-screw hot-melt compounding with a 40:1 L/D extruder and a liquid injection port located after the first melting zone, Liquid Eastman 1020 is added by a gravimetric liquid feeder with a mass-flow tolerance of 0.5–1.0% to avoid feed-rate oscillations that produce die-lip build-up. Moisture in SIS or SBS feedstock above 0.1% by ASTM D6304 Karl Fischer titration causes micro-foaming at the slot die and reduces coating weight uniformity below ±2% on nonwoven lines running at 300–500 m/min. In such cases, the elastomer is pre-dried in a desiccant dryer at 60–70°C for 4–6 h when ambient relative humidity exceeds 60%, and the liquid resin is kept in a closed, nitrogen-blanketed storage vessel to prevent water ingress and oxidative color pickup.
Melt temperature in the extruder is typically maintained between 130°C and 170°C. Prolonged residence time above 180°C accelerates oxidative gel formation in SIS systems; therefore, melt-temperature monitoring at the melt pump is used to prevent excursions above 170°C. When the resin is added as a partial replacement for solid C5 tackifier, screw torque drops in proportion to the liquid loading, but shaft speed may need to be reduced to maintain consistent specific mechanical energy input and avoid overwetting polymer pellets in the feed zone. Gear pumps with internal clearances of 50–75 µm are used to avoid bypass flow at low viscosity. Batch-to-batch viscosity variation for liquid C5 resins is typically controlled within ±10% of nominal; this is sufficient for gravimetric liquid feeders but requires compensation when a Coriolis mass-flow meter is used in continuous coating.
At 25°C, viscosity drift beyond ±15% can alter the relative distribution of resin between the SIS midblock and the SIS endblock, changing peel-to-shear balance without a corresponding change in formulation composition. In high-speed label coating, the adhesive remains thermoplastic, and the resin may exude to the surface when the adhesive is stored on silicone-coated release liners at temperatures above 35°C. For solvent-borne pressure-sensitive adhesives, aromatic solvent addition is not required for typical SIS or SBS hot-melt systems; aliphatic or dearomatized blends with an aniline point above 60°C are preferred for low-color retention.
Regulatory screening for the neat resin should reference supplier documentation rather than generic hydrocarbon-resin assumptions. The resin may be evaluated for indirect food contact under 21 CFR 175.105 as a component of an adhesive, but the formulated adhesive must meet end-use extraction limits; the neat resin itself does not automatically carry food-contact clearance. For European Union applications, REACH registration status and SVHC content should be confirmed against the current safety data sheet. The product contains no added halogens or heavy-metal stabilizers. Table 2 summarizes the principal quality and compliance test designations applicable to inbound release and formulation qualification.
| Assessment | Standard or Regulatory Reference | Required for |
|---|---|---|
| Softening point | ASTM E28 | Release specification and inbound QC |
| Gardner color | ASTM D1544 | Color stability in label adhesives |
| Brookfield viscosity | ASTM D2196 / ISO 2555:2018 | Pump sizing and feed-line design |
| Flash point | ASTM D93 / ISO 2719 | Storage and hot-melt unit safety |
| Moisture content | ASTM D6304 | Moisture-related die foaming control |
| Indirect food contact | 21 CFR 175.105 formulated adhesive | Food-packaging label adhesives |
| REACH SVHC screening | Regulation (EC) 1907/2006 | EU compliance |
The material should not be stored in carbon steel vessels for extended periods at temperatures above 50°C; stainless steel or nitrogen-blanketed carbon steel is preferred to limit viscosity drift. Exposure to copper or copper alloys accelerates oxidative discoloration. In bulk handling, the resin should not be mixed with chlorinated solvents or strong oxidizing agents. If the product is held at low temperature, viscosity increases and pumping requires a heater with a maximum skin temperature of 150°C to avoid localized thermal degradation. Storage at sub-zero temperatures is not required, but the product should be blanketed with dry nitrogen when held in heated bulk tanks and protected from sustained temperatures above 150°C.