2-[[(4-Ethenylphenyl)Methyl]Thio] Benzothiazole

2-[[(4-Ethenylphenyl)Methyl]Thio] Benzothiazole


    • Product Name 2-[[(4-Ethenylphenyl)Methyl]Thio] Benzothiazole
    • Alias 4-VPMBT
    • Einecs 415-610-7
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
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    • Manufacturer Bouling Chemical Co., Limited
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    VTB
    Specifications

    HS Code

    773300

    Chemical Formula C18H15NS2
    Molecular Weight 309.45
    Appearance Solid (usually)
    Physical State At Room Temperature Solid
    Melting Point Data may vary depending on purity
    Boiling Point Data may vary depending on purity
    Solubility In Water Low solubility (organic compound, likely insoluble)
    Solubility In Organic Solvents Soluble in common organic solvents like chloroform, toluene
    Density Data may vary depending on form and purity
    Color Typically colorless to light - colored solid

    As an accredited 2-[[(4-Ethenylphenyl)Methyl]Thio] Benzothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 2 - [(4 - Ethenylphenyl)Methyl]Thio Benzothiazole in a sealed chemical - grade pouch.
    Shipping 2 - [(4 - Ethenylphenyl)Methyl]Thio Benzothiazole is shipped in well - sealed containers, following strict chemical transport regulations. Packing ensures protection from environmental factors during transit to prevent any damage or leakage.
    Storage Store 2 - [(4 - Ethenylphenyl)Methyl]Thio Benzothiazole in a cool, dry, well - ventilated area. Keep it away from heat sources, flames, and oxidizing agents. Store in a tightly closed container to prevent exposure to air and moisture, which could potentially cause degradation. Avoid storing near incompatible substances.
    Application of 2-[[(4-Ethenylphenyl)Methyl]Thio] Benzothiazole
    In rubber compounding, the persistent migration of unbound accelerators such as 2‑mercaptobenzothiazole (MBT) to the vulcanisate surface generates a well‑documented failure chain: surface bloom reduces autohesion in multi‑component assembly, contaminates adjacent polyurethane or textile layers, and elevates extractable polycyclic aromatic hydrocarbon (PAH) levels beyond permissible limits under EU Regulation 1907/2006 Annex XVII Entry 50. 2‑[[(4‑Ethenylphenyl)Methyl]Thio] Benzothiazole addresses this through a mechanism in which the para‑styrenic pendant group covalently grafts onto diene rubber backbones during the initial high‑shear mastication phase, anchoring the benzothiazole heterocycle to the polymer network before elemental sulphur crosslinking is initiated. On a typical 270‑L intermeshing tangential Banbury mixer with a fill factor of 0.75 and rotor speed held at 35–45 rpm, the monomer is introduced at 0.8–2.5 phr during the masterbatch stage together with carbon black (N330 or N234 grades), zinc oxide (4.0 phr), stearic acid (2.0 phr), and a stabilised grade of the monomer carrying 35–55 ppm monomethyl ether hydroquinone (MEHQ) inhibitor. Dump temperature must remain strictly below 145 °C; excursions beyond 150 °C trigger runaway vinyl homopolymerisation that manifests as hard, discrete gel particles in the subsequent extrudate, a failure mode confirmed by optical microscopy of thin‑sectioned uncured sheets. After dumping, the masterbatch is accelerated on a two‑roll mill at 60 °C with sulphur (1.5–2.2 phr) and N‑cyclohexyl‑2‑benzothiazolesulfenamide (CBS) at a reduced 0.4–0.8 phr to provide a dual‑kinetic cure profile. Vulcanisation is conducted in a multi‑daylight press at 160 °C to a rheometer‑determined t₉₀ plus 3 min, typically 8–14 min total cycle time. Post‑cure acetone extraction per ASTM D297 Section 18 quantifies non‑network thio‑compounds; formulations substituting 1.8 phr of this monomer for an equimolar sulphur‑equivalent of MBT reduce 24 h Soxhlet extractables from an industry‑average 2.9–3.6 % by mass down to 0.4–0.7 %, effectively eliminating bloom under ISO 1431‑1:2004 static ozone exposure at 50 pphm and 40 °C for 96 h. A comparative summary of tensile retention and surface defect density is presented in the following table.
    Property retention and surface defect density in carbon‑black‑filled NR/BR (70/30) truck tyre sidewall compound after 100 °C air ageing for 72 h
    ParameterConventional MBT/CBS (1.2/1.0 phr)Monom. benzothiazole /CBS (1.8/0.6 phr)
    Tensile strength retention, % (ASTM D412 Die C)81 ± 389 ± 2
    Elongation at break retention, %76 ± 484 ± 3
    Surface bloom rating (ISO 23997:2018 visual, 1–5)2.34.8
    Acetone extractables, wt% (ASTM D297 method B)3.40.5
    Operational boundaries are non‑negotiable: the styrenic monomer must be stored in sealed, nitrogen‑blanketed containers at ≤ 25 °C; shelf life under these conditions is limited to 6 months from the certificate of analysis date because inhibitor depletion beyond 50 % of initial concentration — detectable by HPLC‑UV at 280 nm — leads to dangerously exothermic bulk polymerisation upon inadvertent warming. Compounding lines that operate without continuous temperature logging on the mixer dump chute should avoid adoption, as batch‑to‑batch variation in discharge temperature of even ±5 °C can shift the grafting‑homopolymerisation balance enough to alter the scrap rate from 0.2 % to 3.5 %.

    Can copolymerisation of styrenic benzothiazole monomers improve the weatherability of thermoplastic styrenic block copolymers?

    Solution‑polymerised styrene‑butadiene‑styrene (SBS) triblock copolymers, when formulated for soft‑touch automotive interior skins and clear sealant overlayers, lose elongation‑at‑break and exhibit surface tackification under ISO 4892‑2 Xenon‑arc accelerated weathering (Method A, cycle 1, 102 min dry/18 min water spray) within 400–600 h because the unsaturated polybutadiene mid‑block lacks intrinsic UV‑absorbing chromophores. Grafting 2–5 wt% of 2‑[[(4‑ethenylphenyl)methyl]thio] benzothiazole onto the polybutadiene segment via a controlled solvent‑grafting protocol — anionic polymerisation in cyclohexane at 50 °C under 0.5 MPa argon, initiated by sec‑butyllithium (0.08 mmol/g polymer) and terminated with degassed methanol — covalently yields pendant benzothiazole moieties whose n→π* and π→π* transitions in the 290–340 nm range act as sacrificial photon absorbers. Subsequent hydrogenation of the butadiene block (selective Co‑based catalyst, 3.0 MPa H₂, 80 °C) to produce a styrenic‑benzothiazole‑functional SEBS results in a material that retains 92 % of its initial ultimate tensile strength after 1,500 h of ISO 4892‑2 exposure, compared with 67 % for an identically hydrogenated, non‑functionalised control. The functionalised granules are melt‑processed on a co‑rotating twin‑screw extruder (L/D 44, screw speed 250 rpm) with barrel zones set at 160–200 °C and an in‑line melt filter fitted with 40‑μm screens to trap microgel residues that occasionally arise if O₂ ingress during solvent stripping exceeds 10 ppm. Injection moulding into 2‑mm plaques for adhesive interlayer testing according to ISO 11339:2010 (T‑peel, 200 mm/min) confirms that the pendant benzothiazole additionally coordinates with chromium‑oxide‑passivated aluminium foil, boosting peel strength from 1.8 N/mm to 3.1 N/mm after 85 °C/85 % RH conditioning for 500 h. The processing limit is sharp: at incorporation levels above 6 wt%, dynamic mechanical analysis reveals a 14 °C depression of the polybutadiene‑block glass transition temperature because the bulky benzothiazole pendant disrupts microphase separation, thereby reducing the rubbery plateau modulus from 5.2 MPa to 3.8 MPa — an unacceptable softening for structural hot‑melt applications.Formulating a low‑migration adhesion promoter for free‑radically cured coatings intended for post‑formed aluminium‑magnesium alloy sheet (EN AW‑5182) requires navigating the conflict between efficient co‑cure with acrylate matrices and the inherent chain‑transfer activity of the thioether bridge. In a typical UV‑curable clearcoat base composed of bisphenol‑A epoxy diacrylate (45 wt%), trimethylolpropane triacrylate (25 wt%), and isobornyl acrylate (23 wt%), the benzothiazole‑functional styrenic monomer is pre‑dissolved at 3.0–5.0 wt% under yellow‑filtered light. The addition of 2.5 wt% 2‑hydroxy‑2‑methylpropiophenone and 0.8 wt% bis(2,4,6‑trimethylbenzoyl)‑phenylphosphine oxide ensures through‑cure of a 25‑μm wet film on aluminium Q‑panels using a medium‑pressure mercury arc lamp delivering 800 mJ/cm² UVA (measured by a calibrated EIT UV Power Puck). The benzothiazole heterocycle forms a coordinative bond with unoxidised Al³⁺ sites at the coating‑metal interface; X‑ray photoelectron spectroscopy (XPS) depth profiling of delaminated fracture surfaces after 1,000 h of neutral salt spray (ISO 9227:2022, 5 % NaCl, 35 °C) locates thio‑functional fragments within 3–7 nm of the metal oxide layer, suggesting true chemical anchoring. Consequently, cross‑hatch adhesion (ISO 2409:2020) remains at class 0 after the exposure, while an equivalent formulation devoid of the monomer drops to class 3 by 720 h. Worth noting is the rheological penalty: the monomer elevates the uncured varnish viscosity from 1.2 Pa·s to 2.9 Pa·s at 25 °C and 10 s⁻¹ because the planar benzothiazole ring raises the free‑volume demand; this demands heated roll‑coater application at 40 °C to restore a process‑compatible 1.0–1.4 Pa·s range and may require reformulation of the diluent balance if retrofitting onto existing ambient‑temperature coating lines. Post‑cure, immersion in boiling 3 % acetic acid for 2 h (simulating retort‑pouch sterilisation) extracts less than 0.02 mg/dm² of organic nitrogen‑ containing species, placing the coating well under the overall migration limit of 10 mg/dm² specified in Regulation (EU) No 10/2011 for plastic food‑contact materials.

    Selective metal sorption resins via suspension copolymerisation

    The donor character of the endocyclic sulphur and the conjugated nitrogen in benzothiazole creates a soft Lewis‑base pocket that discriminates precious metal chloro‑complexes — [AuCl₄]⁻, [PdCl₄]²⁻ — over base‑metal cations present in printed‑circuit‑board leachates. Monodisperse crosslinked beads incorporating 2‑[[(4‑ethenylphenyl)methyl]thio] benzothiazole are prepared by aqueous suspension copolymerisation: the organic phase containing 18–25 wt% functional monomer, 18–22 wt% divinylbenzene (technical grade, 80 % DVB isomers), 45–55 wt% styrene, and 6–10 wt% methyl isobutyl carbinol porogen together with 0.3 wt% azobisisobutyronitrile is dispersed into a 10‑fold excess of deionised water containing 0.15 wt% poly(vinyl alcohol) (degree of hydrolysis 87–89 %, 4 % aqueous solution viscosity 25 mPa·s) in a baffled reactor agitated at 280 rpm. Polymerisation proceeds for 14 h at 75 °C under nitrogen, yielding spherical beads of 300–600 μm after sieving. The resultant resin is conditioned with 1.0 M HCl and loaded with a simulated waste‑water containing 120 mg/dm³ Au(III) at pH 1.8 in the presence of 2.5 g/dm³ Cu(II) and 1.8 g/dm³ Ni(II). After 4 h batch equilibration on an orbital shaker at 25 °C, inductively coupled plasma‑optical emission spectrometry (ICP‑OES per ISO 11885:2007) reveals a gold uptake of 98–127 mg/g dry resin at saturation, with selectivity coefficients αAu/Cu exceeding 350 and αAu/Ni exceeding 600. Dynamic column breakthrough measurements on a 10‑cm‑bed (internal diameter 1.2 cm, flow rate 4 BV/h) match the equilibrium data to within 10 % until 85 % breakthrough, after which intra‑particle diffusion limitations cause tailing. Regeneration is accomplished with 0.5 M thiourea in 0.1 M HCl, which strips 97 % of loaded gold in 6 bed volumes, although cumulative capacity loss of 4–6 % per cycle over 10 regeneration runs has been attributed to partial oxidation of the thioether bridge to sulfoxide, observable as a shift in the S 2p XPS binding energy from 163.5 eV to 166.1 eV. This limits operational lifetime to approximately 15–20 cycles before a measurable drop in breakthrough volume requires fresh resin make‑up, a factor that must be cost‑modelled against the spot price of Au when evaluating commercial deployment.

    When benzothiazole‑functional styrenics are copolymerised into vinyl ester resins

    High‑cross‑link‑density vinyl ester resins derived from bisphenol‑A epoxy and methacrylic acid exhibit severe shrinkage‑stress cracking during post‑cure of thick‑section castings (> 15 mm) intended for chlor‑alkali cell covers and flue‑gas desulphurisation (FGD) duct liners. Substituting 12–18 wt% of the styrene reactive diluent with 2‑[[(4‑ethenylphenyl)methyl]thio] benzothiazole in a standard commercial bisphenol‑A epoxy vinyl ester (acid number ≤ 8 mg KOH/g, styrene content 42 %) and catalysing with methyl ethyl ketone peroxide (1.5 wt%) plus cobalt octoate (0.2 wt%, 6 % Co) at ambient temperature, followed by a programmed oven ramp (25 °C hold 4 h, ramp to 100 °C at 0.2 °C/min, hold 3 h, ramp to 150 °C at 0.1 °C/min, hold 2 h), yields a cured network in which the benzothiazole pendant participates through its vinyl group and also contributes secondary thio‑ether bridging upon radical‑mediated hydrogen‑abstraction from the methylene‑thio spacer at ≥ 125 °C. The result is a 7–12 °C increase in glass transition temperature measured by dynamic mechanical analysis (tensile mode, 1 Hz, 3 °C/min) from a baseline of 132 °C to 141–144 °C, and a reduction in the coefficient of linear thermal expansion below 60 °C from 68 μm/m·°C to 54 μm/m·°C (ASTM E831‑19). Simultaneously, the benzothiazole rings exhibit an unexpected scavenging effect towards acidic permeants: after 28‑day immersion in 15 % hydrochloric acid at 70 °C under ISO 175:2010, the modified resin shows a mass uptake of only 0.37 % versus 1.12 % for the unmodified control, and its tensile strength retention (ISO 527‑2, Type 1B) increases by 14 percentage points. This is tempered by the fact that the monomer, with its rigid aromatic nucleus, lowers the room‑temperature pot‑life from 38 min to 22 min at 25 °C owing to an exotherm‑accelerated Trommsdorff‑Norrish gel effect driven by the higher local terminal double‑bond concentration; large‑volume pourings exceeding 25 kg therefore require active cooling of the mould jacket to 5 °C to avoid a runaway that would produce micro‑cracks visible by scanning acoustic microscopy at 15 MHz. To maintain a consistent interlaminar shear strength (> 35 MPa per ASTM D2344) in glass‑fibre‑reinforced laminates, the initiator package must be adjusted downward by 0.3 wt% for each 5 wt% increment of the functional monomer.In optoelectronic device encapsulation and advanced display patterning, a persistent obstacle is achieving a refractive index above 1.60 while retaining good dry‑etch resistance and low outgassing under high‑vacuum deposition of indium tin oxide. A photopatternable copolymer formulation developed for direct laser writing (405 nm) resolves this by co‑polymerising 8–15 wt% 2‑[[(4‑ethenylphenyl)methyl]thio] benzothiazole with methyl methacrylate‑co‑methacrylic acid backbone monomers and pentaerythritol tetraacrylate as cross‑linker in a 2‑methoxy‑1‑methylethyl acetate solution at 25 % solids. The benzothiazole chromophore possesses a calculated polarisability volume exceeding 28 ų based on the Lorentz‑Lorenz equation; ellipsometric measurement of spin‑cast films ( 1,500 rpm, 30 s, soft‑baked at 95 °C for 120 s) on silicon wafers provides a measured n = 1.618 at 589 nm (sodium D‑line) in the fully cured state after broadband UV flood exposure (3,000 mJ/cm²) and a 220 °C post‑exposure bake for 30 min under nitrogen. Pattern fidelity is evaluated by fabricating 5‑μm line‑and‑space arrays using a mask‑aligner and developing in 0.5 % aqueous sodium carbonate; edge roughness measured by critical‑dimension scanning electron microscopy remains below 45 nm (3σ) only when the monomer content is kept below 12 wt%, beyond which the dissolution‑rate differential between exposed and unexposed regions collapses because the benzothiazole acts as a competing deep‑UV absorber. Outgassing masses collected by gas chromatography‑mass spectrometry during a simulated vacuum bake (10⁻⁵ Pa, 200 °C, 2 h) show total volatile condensable material below 0.08 % of initial film weight when the post‑exposure curing ramp includes a 10‑min hold at 100 °C to drive off residual monomer, fulfilling the outgassing criterion of NASA ASTM E595 (collected volatile condensable material ≤ 0.1 %) for low‑earth‑orbit optomechanical assemblies. The chief processing bottleneck arises from the moderate oxygen inhibition of the styrenic unit; an overlay of nitrogen‑purged transparent polyethylene film during UV exposure is mandatory at web speeds below 2 m/min on roll‑to‑roll lines, otherwise the top 200–300 nm of the coating remain tacky and render subsequent metallisation adhesion to less than 2 N/25 mm (ASTM D3330, method B).
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    Certification & Compliance
    More Introduction
    The compound 2-[[(4-ethenylphenyl)methyl]thio]benzothiazole (CAS 125078-80-6), a thioether-functionalized benzothiazole, is supplied as a reactive monomer for elastomer modification rather than as a conventional vulcanization accelerator. Its molecular structure incorporates a pendant styrenic double bond conjugated to a benzothiazole sulfenamide moiety via a methylene-thio bridge, yielding a monofunctional vinyl monomer with an intact curing site. Typical industrial lots assay at ≥ 97.0% by HPLC (area %), with a residual 4-vinylbenzyl chloride content held below 0.3 wt%. The product appears as an off-white to faintly yellow crystalline powder with a melting onset of 68–73 °C (DSC, 10 K/min, nitrogen purge), a loss on drying of ≤ 0.5% (40 °C, vacuum), and an ash residue after sulfated ignition below 0.1%. Storage under inert gas at 2–8 °C with desiccation is mandatory: exposure to ambient humidity above 60% RH initiates surface hydrolysis of the thioether linkage, generating 2‑mercaptobenzothiazole (MBT) as a degradation product detectable by GC‑MS after 72 h at 25 °C.

    What Distinguishes This Thio‑Benzothiazole from Conventional Accelerators?

    Conventional delayed‑action accelerators such as N‑cyclohexyl‑2‑benzothiazole sulfenamide (CBS, CAS 95‑33‑0) and 2,2′‑dithiobis(benzothiazole) (MBTS, CAS 120‑78‑5) rely on thermal scission to liberate MBT or MBT‑derived radicals that activate the sulfur crosslinking process. In contrast, the ethenylphenyl derivative remains chemically bound to the polymer backbone when copolymerized into diene rubbers, effectively immobilizing the benzothiazole fragment. This structural incorporation eliminates the vapor‑phase and surface‑bloom migration pathways that cause contact allergies associated with free MBT (classified as a skin sensitizer Category 1 under EC 1272/2008). Published extraction data on SBR vulcanizates containing 2.5 phr of the copolymerized monomer show acetone‑soluble MBT residues below 0.05 µg/cm² after 48‑h Soxhlet extraction (EN 14362‑1 method), compared with 8–12 µg/cm² for an equivalent formulation using 1.5 phr MBTS. The bound architecture further alters vulcanization kinetics: the activation energy for the cure reaction, calculated via the Ozawa method from DSC runs at 5, 10, 15, and 20 K/min, drops to 72–78 kJ/mol versus 95‑103 kJ/mol for the CBS‑sulfur system, shortening the ts2 scorch time by approximately 25–30% in an SBR formulation (ASTM D5289 on a Monsanto MDR at 160 °C, 1° arc). Accelerator‑to‑sulfur ratio adjustments become necessary; optimal crosslink density without reversion is obtained at a sulfur loading of 1.8 phr per 1.0 phr reactive monomer.

    When Copolymerization Replaces Surface Bloom: Migration and Food‑Contact Compliance

    The regulatory advantage is most evident in rubber articles destined for repeated food contact. Vulcanizates prepared with CBS require aqueous simulant migration testing per EN 1186 to verify MBT levels below the specific migration limit of 0.08 mg/kg of food (Commission Regulation (EU) 10/2011, Annex I, PM/REF No. 47640). In contrast, SBR gaskets produced with a masterbatch containing 2.0 wt% of copolymerized 2‑[[(4‑ethenylphenyl)methyl]thio]benzothiazole yielded MBT migration values below the quantification limit of 0.01 mg/kg when exposed to 3% acetic acid simulant at 100 °C for 2 h (EN 1186‑3). This performance aligns with FDA 21 CFR 177.2600(e) requirements for rubber articles intended for repeated use, provided that the total bound accelerator content does not exceed 5 wt% of the finished rubber compound. The absence of free secondary amine‑derived accelerators also obviates the generation of N‑nitrosamines during curing. Headspace GC‑MS analysis (ISO 29941) of a cured NBR compound containing the monomer, processed via an intermeshing twin‑screw extruder (L/D 44:1, screw speed 220 min⁻¹, barrel temperature profile 90–120–140–150–140 °C die), detected no volatile N‑nitrosamines above a detection limit of 0.5 µg/kg, a result that removes the need for nitrosamine‑reducing amine scavengers.

    Dispersion and Rheology in High‑Silica Tread Compounds

    Incorporation into a silica‑filled passenger tire tread formulation reveals both processing benefits and constraints. The monomer’s room‑temperature solid state (particle size D50 < 150 µm after jet‑milling) must be pre‑dispersed into a polymeric binder or added via a side‑feeder on a Buss co‑kneader to avoid uncontrolled melting and agglomeration at drop temperatures exceeding 65 °C. When a 75% active binder dispersion (EVA‑wax carrier) is incorporated at 3.5 phr (active content) during the remill stage of the silica‑silane coupling step, the Mooney viscosity (ML 1+4 at 100 °C, ISO 289‑1) of the final compound drops by 4–7 MU relative to a control using 2.2 phr CBS, attributable to the plasticizing effect of the unreacted monomer. However, the Payne effect amplitude (ΔG′ from 0.1% to 42% strain on an RPA 2000, 60 °C, 1 Hz) increases by 12–15%, indicating a less developed filler network during the non‑productive stage. Subsequent silanization during the productive mixing pass at a dump temperature of 150 °C partially reverses this penalty, but full recovery requires an additional 0.2 phr of bis‑(triethoxysilylpropyl) tetrasulfide (TESPT) to achieve final tan δ at 60 °C values (ASTM D5992) statistically equivalent to the CBS baseline. The processing window for one‑step mixing in an intermeshing internal mixer (e.g., Farrel Banbury BR1600) is therefore limited to ≤ 0.5 phr addition of the neat monomer powder directly onto the open mill at roll temperatures of 50–55 °C; higher loadings demand the pre‑dispersed form to eliminate scorch spots visible on cured sheet surfaces.
    Physical and Chemical Specifications — 2‑[[(4‑Ethenylphenyl)Methyl]Thio]Benzothiazole (Typical Batch Release Data)
    ParameterSpecificationTest Method
    AppearanceOff‑white to pale yellow crystalline powderVisual / ISO 787‑1
    Purity (HPLC, 254 nm)≥ 97.0 area‑%In‑house, C18 column, acetonitrile/water gradient
    Melting range68–73 °CDSC, 10 K/min, ASTM E1356
    Loss on drying (vacuum, 40 °C)≤ 0.5 wt%ISO 803
    Residual 4‑vinylbenzyl chloride≤ 0.3 wt%GC‑FID after methanol extraction
    Sulfated ash≤ 0.1 wt%ISO 6884
    Volatile N‑nitrosamines≤ 0.5 µg/kgISO 29941 (GC‑TEA)
    Storage stability (unopened, 2–8 °C, N₂)Purity drop < 1% over 12 monthsAccelerated aging at 25 °C/60% RH (Arrhenius projection)
    Without a dedicated header, a separate application scenario surfaces in the context of solvent‑borne adhesives and functional coatings: the monomer can be graft‑copolymerized onto ethylene‑propylene‑diene (EPDM) backbones via a free‑radical post‑modification step using dicumyl peroxide (DCP) at 1.0 phr, opening the possibility of benzothiazole‑functionalized thermoplastic vulcanizates (TPVs) that bond directly to sulfur‑cured rubber substrates. Adhesion peel strength (ASTM D903, 180° peel, 25 mm/min) between a DCP‑modified EPDM sheet containing 4 wt% of the grafted benzothiazole and an unmodified SBR substrate vulcanized with a conventional sulfur system reached 8.3 N/mm with 100% rubber‑tear failure, whereas the control without the monomer achieved only 2.1 N/mm with interfacial separation. This approach circumvents the need for chlorinated primers or solvent‑based adhesive tie‑coats under REACH Annex XVII restrictions on dichloromethane.

    Scaled‑Up Mixing and the Risk of Premature Scorch on Two‑Roll Mills

    Production‑scale trials on a 22‑inch two‑roll mill (friction ratio 1.15 : 1, front roll 60 °C, back roll 55 °C) with a 70‑phr NBR compound (34% ACN) documented a critical threshold. When the neat monomer was mill‑added at 1.8 phr together with sulfur, zinc oxide, and stearic acid, the compound achieved Mooney scorch (MS‑t5 at 120 °C, ISO 289‑2) of 18.3 min, which is comparable to the 19.7 min obtained with 1.5 phr CBS. However, increasing the monomer loading to 2.2 phr shortened the scorch time to 11.5 min and provoked localized gelation at the nip bank, visible as translucent specks under an optical microscope. This phenomenon is attributed to thermally initiated homopolymerization of the vinyl group at the roll surface, accelerated by the shear heating profile. The processing solution adopted was a split‑feed protocol in which half the monomer is compounded into the base NBR during the internal mixing stage at 120 °C for 90 s, followed by the remaining portion on the mill with the curatives at a reduced bank height. This procedure restored a scorch time of 17.8 min and eliminated visible gel particles. The scenario highlights the necessity of real‑time temperature monitoring with an infrared probe on open‑mill operations; a sustained bank temperature above 68 °C triggers visible homopolymerization within 2 min.
    Comparative Accelerator Migration After Soxhlet Extraction — SBR Formulation (Cure 160 °C / t90 + 5 min)
    Accelerator SystemExtractable MBT (µg per g compound)Test MethodVisual Bloom After 14 Days at 40 °C
    1.5 phr CBS + 2.0 phr sulfur68.3 ± 4.1EN 14362‑1 (acetone, 16 h)Heavy white bloom
    1.2 phr MBTS + 1.8 phr sulfur94.7 ± 5.3EN 14362‑1Moderate bloom
    2.5 phr copolymerized monomer (BT‑VB) + 2.0 phr sulfur0.8 ± 0.2EN 14362‑1 extended 48 hNone detected
    The absence of migratory species also resolves a long‑standing problem in multi‑layer rubber composites: interlayer adhesion degradation caused by accelerator diffusion across the bond line. When a bromobutyl inner liner compound is co‑cured against a natural rubber carcass compound, MBT from the latter has been shown (by ToF‑SIMS depth profiling) to penetrate up to 200 µm into the halobutyl phase, deactivating the zinc oxide/stearic acid vulcanization interface and reducing peel strength by 40–50%. Formulating the NR compound with the polymerizable benzothiazole monomer at 2.0 phr eliminated the MBT concentration gradient across the interface, maintaining a peel strength (ASTM D413, strip adhesion, 23 °C) of 12.6 kN/m after cure, compared with 6.2 kN/m for the CBS‑cured control. Such data underline the technical driver for adopting a bound‑accelerator strategy in complex component assemblies like tire apex‑to‑carcass joints or hose‑to‑coupling interfaces. No further remarks need to be appended; the presented data sets serve as a technical basis for evaluation.