| HS Code | 932628 |
| Polymer Type | Styrene-Isoprene-Styrene (SIS) block copolymer |
| Block Structure | Linear triblock |
| Styrene Content | 22% |
| Diblock Content | 17% |
| Density | 0.92 g/cm³ |
| Melt Flow Rate | 9 g/10 min at 200 °C/5 kg |
| Hardness | 40 Shore A |
| Tensile Strength | 20 MPa |
| Elongation At Break | 1200% |
| Solution Viscosity | 800 cP at 25% in toluene |
| Appearance | Clear |
| Form | Pellets |
As an accredited Kraton Kraton™D SIS D1111 K factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically supplied in 25 kg (55 lb) bags, palletized and wrapped for industrial storage and handling of Kraton D SIS D1111 K. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Kraton™ D SIS D1111 K, securely palletized in dry conditions and compliant with regulations. |
| Shipping | Shipping description: Kraton™ D SIS D1111 K, solid styrene-isoprene-styrene block copolymer. Non-hazardous and not regulated for transport; no UN number or hazard class assigned. Ship in sealed, labeled containers, protected from moisture, heat, and ignition sources; follow the SDS and carrier/local regulations. |
| Storage | Store Kraton™ D SIS D1111 K in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed and protect contents from moisture, dust, and contamination. Use original packaging, avoid prolonged high-temperature or UV exposure, and follow local regulations and the safety data sheet. |
| Shelf Life | Shelf life is 36 months from manufacture when stored in original, unopened packaging under dry, cool conditions. |
In disposable hygiene construction lamination lines running above 300 m/min with nonwoven web tensions of 2–8 N/50 mm, Kraton™ D SIS D1111 K is compounded into hot-melt pressure-sensitive adhesives for polyethylene backsheet bonding, acquisition-layer attachment, and elastic-strand anchoring. The polymer is formulated at 25–35 wt% with a hydrogenated C5 tackifier having a ring-and-ball softening point of 95–105°C per ASTM E28-18, 15–25 wt% naphthenic process oil with pour point below -20°C, and 1–2 wt% of a hindered phenolic/phosphite antioxidant package. Mixing is performed in a heated sigma-blade mixer or a twin-screw extruder with L/D ≥ 40, barrel temperatures between 150°C and 180°C, and melt residence time below 90 s; excursions above 180°C in the presence of atmospheric oxygen accelerate oxidative scission of the unsaturated isoprene midblock and produce viscosity drift exceeding ±10% at 160°C when measured by a Brookfield RV DVII Thermosel according to ASTM D3236-15. The nominal 18 wt% diblock content of D1111 K reduces die swell and accelerates wet-out on low-energy polyolefin films, while the styrene domains provide room-temperature cohesion against pad-attachment creep at 40–50°C warehouse storage. Slot-die coating through 0.8–1.2 mm shims at coatweights of 3–8 g/m² is used for continuous lamination because the lower surface-to-volume ratio limits thermal history; spiral-spray manifolds operating at 6–10 bar atomizing air apply discontinuous elastic-strand adhesive at 2–4 g/m². Lot release is based on differential scanning calorimetry glass transition onset at 10 K/min per ISO 11357-2:2020; a styrene endotherm shift greater than ±2°C is treated as a compounding fault.
At 35–45 wt% solids in toluene or a toluene/ethyl acetate blend, D1111 K pressure-sensitive adhesives are prepared with a high-torque dissolver at tip speed 15–25 m/s until a drawdown chip test shows no undissolved polymer or rosin ester particles. The solution is let down to 2,000–5,000 mPa·s at 25°C for reverse-roll or comma coating onto BOPP, polyester, or crepe paper facestocks. A typical formulation contains 100 phr D1111 K, 80–120 phr rosin ester with acid number below 15 mg KOH/g, 1–2 phr antioxidant, and 0.5–1.5 phr fumed silica as an anti-blocking and matting agent. Coaters operating at 80–150 m/min dry the adhesive in zoned ovens with first-stage air temperature below 60°C to prevent skin-over, mid-stage 90–110°C, and final-stage 130–150°C; residual toluene in the dried film is checked by headspace gas chromatography per ISO 11890-2:2020 and kept below 1,000 mg/kg for industrial tape grades. The peel-to-shear balance is governed by the tackifier-induced shift in glass transition temperature and by entanglement density remaining after solvent removal; loop tack per FINAT FTM 9 typically declines when rosin ester exceeds 120 phr because dilution of the styrene network raises room-temperature damping factor. Shear holding power to stainless steel is measured per FINAT FTM 8 with a 25 mm × 25 mm contact area and 1 kg load; failure before 24 h at 40°C rejects a batch for masking-tape use. End products include industrial masking tapes, surface-protection films, and appliance graphic labels. Regulatory controls include the EU Industrial Emissions Directive 2010/75/EU Annex VII Part 4 for coating lines above solvent consumption thresholds, REACH Annex XVII restrictions on toluene in consumer adhesives, and FDA 21 CFR 175.105 for indirect food-contact packaging tape where the dried adhesive article includes a functional barrier. Published data for this exact D1111 K/rosin ester/oil ternary is limited to supplier technical literature; full factorial design-of-experiment validation is required for customer-specific facestocks and silicone release liners.
| D1111 K (phr) | Rosin ester (phr) | Naphthenic oil (phr) | Processing observation | Controlling test |
|---|---|---|---|---|
| 100 | 80 | 10 | Higher cohesion; reduced adhesive residue on BOPP in shear | FINAT FTM 8 |
| 100 | 100 | 15 | Balanced peel and tack for industrial masking | FINAT FTM 9, ASTM D3330 |
| 100 | 120 | 20 | Low-viscosity solution; increased cold flow on vertical surfaces | ASTM D3330, FINAT FTM 8 |
Electron-beam irradiation of D1111 K-based pressure-sensitive adhesive films exploits residual unsaturation in the polyisoprene midblock to generate a solvent-free crosslinked network without peroxide decomposition products. On reel-to-reel EB lines operating at accelerating voltages of 80–120 kV for adhesive coatings of 20–50 g/m², absorbed doses between 30 kGy and 60 kGy are selected; doses below 30 kGy produce insufficient gel fraction for high-temperature masking tapes, while doses above 80 kGy can embrittle the styrene domains and create edge curl on silicone-coated paper liners. D1111 K is first hot-melt coated or solvent coated and dried, then passed through the electron beam; the unsaturation of the isoprene midblock is sufficient for intermolecular crosslinking without added peroxide, but the nominal 18 wt% diblock fraction limits network perfection, so gel fraction is measured per ASTM D2765-16 by boiling xylene extraction and maintained between 40% and 70% for masking-tape and dicing-tape grades. Dose uniformity is verified with radiochromic film dosimeters calibrated to ±5% across web width; nonuniformity greater than 10% produces uneven delamination on silicone release liners because undercrosslinked edge lanes fail cohesively during unwinding. UV curing of D1111 K with benzophenone-type photoinitiators is generally not used in industrial PSA coating because the isoprene midblock undergoes competing degradation, oxygen inhibition at the exposed surface, and insufficient through-cure at coatweights above 15 g/m²; electron beam remains the standard radiation source. End products include high-temperature automotive masking tapes, electronics dicing tape, and printed circuit board protective films where the cured adhesive must satisfy halogen-free requirements under IEC 61249-2-21:2003 and RoHS 2011/65/EU Annex II substance limits. Exact dose-to-property response for D1111 K-specific formulations is not fully covered in public technical bulletins; converter-side dose mapping is required.
Oxidized bitumen with penetration of 40–60 dmm per ASTM D5/D5M-20 and ring-and-ball softening point of 85–105°C per ASTM D36/D36M-14(2020) is heated to 160–170°C in a horizontal high-shear mixer. D1111 K is introduced at 8–12 wt% of the total compound under rotor speeds of 1,000–1,500 rpm for 60–90 min; the SIS elastomer swells in the maltene fraction and forms an interpenetrating network that improves low-temperature flexibility and reduces cold-flow on vertical below-grade surfaces. The dispersed polymer phase is generated by shear input and viscosity recovery during cooling rather than by filtration; Brookfield viscosity at 160°C should remain below 1,500 mPa·s using thermosel spindle 27 at 10 rpm to allow smooth knife-over-roll or slot-die application. The compound is cooled and applied to a polyester carrier at 90–120°C to produce membranes of 1.5–2.5 mm thickness. Low-temperature flexibility is evaluated by bending a 150 mm × 50 mm strip over a 10 mm mandrel at -15°C per EN 1109:2013; surface cracking before -15°C indicates insufficient polymer wetting or oxidative degradation during mixing. Peel adhesion to primed concrete is measured per ASTM D903-98(2017); industrial self-adhesive modified-bitumen membranes often target values above 10 N/25 mm, but published data for this exact D1111 K/oxidized bitumen binary is limited and full-scale validation on the intended substrate is required. The unsaturated isoprene phase should not be held above 180°C for more than 60 min during storage because oxidative chain scission raises penetration and destroys elastic recovery. End products include below-grade waterproofing membranes, tunnel liners, and plaza deck systems where the membrane must conform to uneven concrete surfaces and resist hydrostatic water ingress.
When D1111 K is evaluated for monolayer cast film in elastic nonwoven laminates, the nominal 18 wt% diblock content lowers melt viscosity but also reduces the load-bearing styrene phase, leading to film blocking on chill rolls and orientation instability at draw ratios above 4:1. Processing on a single-screw extruder with L/D 24–30 and melt temperature 170–185°C requires antiblock masterbatch at 1–2 wt% and a chilled take-off roll set below 15°C to limit neck-in. Published data for this specific D1111 K monolayer configuration is limited; most converters select hydrogenated SEBS or higher-styrene SIS grades for elastic film because D1111 K’s low styrene content yields tension set above 15% after 100% elongation when tested per ASTM D412-16.
In medical tape converting lines requiring clean-peel removal from intact skin, a hot-melt D1111 K compound is normally formulated without high-abietic-acid rosin esters because oxidation products of such resins are associated with contact sensitization. D1111 K is used at 30–40 wt% with a fully hydrogenated hydrocarbon tackifier of softening point 90–100°C per ASTM E28-18, 20–30 wt% white mineral oil complying with Ph. Eur. 10.0 or USP-NF monographs, and 1 wt% hindered phenolic antioxidant; the compound is processed in a jacketed recirculating hot-melt unit at 150–170°C and slot-die coated onto polyurethane film facestock at 25–50 g/m². Peel adhesion to stainless steel per ASTM D3330/D3330M-04(2018) is not sufficient for skin-safety release; the adhesive must undergo in-vitro cytotoxicity per ISO 10993-5:2009 and skin irritation and sensitization per ISO 10993-10:2021, with results assessed under the risk management file required by ISO 14971:2019. The nominal 18 wt% diblock fraction lowers the plateau modulus, which can reduce pain during removal from delicate skin, but it also increases adhesive transfer if peel rates exceed 300 mm/min; cohesive strength is therefore monitored by shear holding power at 37°C with 1 kg load for 24 h. Sterilization compatibility is a critical processing boundary: ethylene oxide exposure at 50–60°C can plasticize the isoprene phase and temporarily lower shear strength, whereas gamma irradiation above 25 kGy can crosslink the unsaturated midblock and shift peel values upward. End products include foam bandage adhesives, wearable glucose sensor mounting tapes, and surgical incise films requiring 24–72 h adhesion without epidermal stripping. Batch release requires endotoxin levels below 0.5 EU/mL per ANSI/AAMI ST72:2019 and no cytotoxicity grade greater than 2 per ISO 10993-5:2009.
| Segment | Regulation/Standard | Clause or test method | Limit or control |
|---|---|---|---|
| Hygiene hot-melt construction | REACH Regulation (EC) No 1907/2006 | SVHC candidate list notification | Substance above 0.1 wt% triggers notification |
| Industrial solvent-borne tape | EU Industrial Emissions Directive 2010/75/EU | Annex VII Part 4 coating solvent emission | Site-specific emission limit value and solvent management plan |
| Electronics dicing tape | RoHS 2011/65/EU | Annex II restricted substances | Pb 1,000 mg/kg; Cd 100 mg/kg; halogen-free limits per IEC 61249-2-21:2003 |
| Medical skin-contact tape | ISO 10993-5:2009, ISO 10993-10:2021 | In vitro cytotoxicity, sensitization, irritation | Cytotoxicity grade ≤ 2; no delayed dermal sensitization |
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Kraton™ D SIS D1111 K is a linear styrene-isoprene-styrene triblock copolymer manufactured by sequential anionic polymerization. The grade carries a nominal polystyrene endblock content of 22 % by weight, with the balance comprising a polyisoprene midblock and a non-staining antioxidant package. The block architecture produces a reversible physical network: the polystyrene endblocks microphase-separate into glassy domains, while the polyisoprene phase retains molecular mobility above its sub-ambient glass transition. This combination provides melt processability in hot-melt equipment, solid-state rubber elasticity, and pressure-sensitive tack. Supplier reference data list a specific gravity of 0.92 when tested to ASTM D792-20. Under ISO 1133-1:2022 or ASTM D1238-20, the melt flow rate is 3.0 g/10 min at 200 °C with a 5 kg piston load. The diblock content is typically controlled to ≤1.0 % by weight, reducing the unattached polyisoprene fraction and supporting cohesive strength in hot-melt pressure-sensitive adhesives.
Compared with styrene-butadiene-styrene block copolymers of similar melt flow, D1111 K provides lower room-temperature modulus and higher tack because the polyisoprene midblock has a lower entanglement modulus than polybutadiene. In loop tack screening conducted according to ASTM D6195-22 or FINAT FTM 9, D1111 K formulations generally show higher tack at low coating weights than SBS-based formulations, but lower shear adhesion failure temperature unless endblock-reinforcing resins are added. Against lower-styrene SIS grades such as D1112 K, the 22 % polystyrene content of D1111 K increases the volume fraction of glassy polystyrene domains and raises the plateau modulus above 60 °C. The practical result is higher cohesive integrity in die-cut labels, tapes, and transfer adhesives exposed to 40 °C to 50 °C storage. Published data for this specific configuration is limited when tackifier aromaticity is not controlled, because a high-aromatic C9 resin can partially reverse the observed differences.
| Parameter | D1111 K | D1112 K | D1113 P |
|---|---|---|---|
| Nominal polystyrene content | 22 % by weight | 15 % by weight | 16 % by weight |
| Melt flow rate at 200 °C/5 kg | 3.0 g/10 min | 5.0 g/10 min | 24 g/10 min |
| Diblock content | <1.0 % by weight | <1.0 % by weight | <1.0 % by weight |
| Typical melt viscosity at 175 °C | Higher than D1112 K | Lower than D1111 K | Substantially lower than D1111 K |
| Primary hot-melt application | Higher-cohesion PSA and die-cut labels | General-purpose PSA | High-speed, low-viscosity coating |
On production-scale hot-melt adhesive lines, the limiting variable for D1111 K is not initial melting but thermo-oxidative degradation of the unsaturated polyisoprene midblock. A continuous single-screw extruder with an L/D ratio of 24:1 to 30:1 and a compression ratio of 3:1 can process the neat polymer at barrel setpoints from 140 °C to 170 °C. Melt residence time above 190 °C should be kept below 20 min to limit gel formation and viscosity drift. Nitrogen blanketing of the feed throat is recommended when transfer lines exceed 2 m. Pellets stored at 60 % RH or higher may carry surface moisture sufficient to produce die foaming. Pre-drying in a desiccant dryer at 60 °C for 2 h reduces visible bubble formation, although the polymer backbone is not hygroscopic. Regrind loads above 20 wt% generally require additional stabilizer because the existing antioxidant package may be partially consumed during prior heat history.
Hot-melt pressure-sensitive adhesive formulations based on D1111 K are built around a ternary system of polymer, midblock-compatible tackifier, and oil. C5 aliphatic hydrocarbon resins are compatible with the polyisoprene midblock; hydrogenated rosin esters improve peel adhesion but may reduce thermal stability at prolonged hold times. A starting formulation window of 100 phr D1111 K, 100 phr to 150 phr C5 resin, and 0 phr to 30 phr white mineral oil is commonly evaluated for permanent and semi-removable label stock. At 175 °C, Brookfield viscosity for these systems generally falls between 1,500 mPa·s and 20,000 mPa·s at 50 rpm; the exact value depends on resin softening point, oil molecular weight, and polymer content. Overtackification above 150 phr produces a measurable loss in room-temperature peel and an increase in glassy modulus. Oil loadings above 30 phr reduce shear holding power as measured by ASTM D3654-23 or FINAT FTM 8, and may plasticize the polystyrene domains sufficiently to lower shear adhesion failure temperature by 5 °C to 15 °C.
Low-viscosity sprayable contact adhesives based on D1111 K can be produced by selecting a low-molecular-weight C5 resin and a naphthenic oil, then dissolving the ternary blend in a solvent system such as methylcyclohexane/ethyl acetate. The polyisoprene midblock requires stabilization during solvent recovery; a non-staining phenolic antioxidant at 0.1 phr to 0.5 phr is typical to suppress chain scission and viscosity drift. The wet adhesive should be filtered through a 60 mesh screen to remove undispersed polymer particles before air-assisted spraying. Drying conditions above 80 °C may cause surface skinning; for a wet coating weight of 120 g/m², oven residence times are normally maintained below 10 min. The sprayed film develops tack after solvent flash-off at 23 °C and can be laminated to low-surface-energy substrates after corona treatment to 38 mN/m to 42 mN/m.
In twin-screw compounding with fillers or polar copolymers, shear sensitivity of the polyisoprene midblock must be separated from temperature-induced degradation. Co-rotating twin-screw extruders with L/D ratios of 40:1 to 48:1 and modular screw designs can disperse D1111 K at screw speeds of 150 rpm to 300 rpm, provided barrel temperatures are limited to 160 °C to 190 °C. Above 300 rpm, viscous heating in kneading blocks can raise melt temperature by 10 °C to 20 °C, moving the melt toward the thermo-oxidative degradation zone. Zinc stearate at 0.05 wt% to 0.2 wt% has been reported to reduce plate-out; amine-based processing aids should be avoided because of accelerated oxidative attack on the unsaturated isoprene backbone. Published data for this specific configuration is limited when the screw design contains aggressive high-shear mixing elements, so process validation on the target line is required. When highly filled formulations are used, the D1111 K feed location should be moved downstream of the main filler feed to allow filler dispersion before the elastomer experiences the maximum shear zone.
Regulatory conformance for D1111 K must be verified against the current supplier certificate and applicable regional food-contact legislation. The grade is referenced for indirect food-contact adhesive applications under 21 CFR 175.105 in the United States when the adhesive is separated from food by a functional barrier. For European Union supply, the polymer is subject to registration under Regulation (EC) No 1907/2006; formulators should confirm that no substance on the candidate list is present above 0.1 % by weight. Under Directive 2011/65/EU, supplier documentation typically indicates that the grade does not intentionally contain restricted heavy metals. Migration testing under EU Regulation (EU) No 10/2011 is not applicable to the raw polymer alone and must be performed on the finished article.
| Reference | Scope | Required documentation |
|---|---|---|
| 21 CFR 175.105 | Indirect food-contact adhesives | Supplier compliance statement |
| Regulation (EC) No 1907/2006 | REACH registration and SVHC declaration | SDS and SVHC certificate |
| Directive 2011/65/EU | RoHS restricted substances in finished articles | Supplier declaration |