2-(Prop-2-Yn-1-Ylsulfanyl)-1,3-Benzothiazole

2-(Prop-2-Yn-1-Ylsulfanyl)-1,3-Benzothiazole


    • Product Name 2-(Prop-2-Yn-1-Ylsulfanyl)-1,3-Benzothiazole
    • Alias Propargylthio-1,3-benzothiazole
    • Einecs 'EINECS 687-758-1'
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    864386

    Chemical Formula C10H7NS2
    Molecular Weight 205.3
    Appearance Solid (predicted)
    Boiling Point Estimated around 335 - 340 °C at 760 mmHg
    Melting Point No data available (experimentally), can be estimated computationally
    Solubility In Water Poorly soluble (due to non - polar nature of the molecule)
    Solubility In Organic Solvents Soluble in common organic solvents like dichloromethane, chloroform, etc.
    Density Estimated around 1.3 - 1.4 g/cm³
    Vapor Pressure Very low at room temperature
    Flash Point Estimated around 156 - 160 °C
    Stability Stable under normal conditions, but may react with strong oxidizing agents

    As an accredited 2-(Prop-2-Yn-1-Ylsulfanyl)-1,3-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-(Prop - 2 - Yn - 1 - Ylsulfanyl)-1,3 - benzothiazole in sealed chemical - grade packaging.
    Shipping The chemical 2-(Prop - 2 - Yn - 1 - Ylsulfanyl)-1,3 - Benzothiazole is shipped in specialized containers, compliant with hazardous chemical regulations. Care is taken to ensure stability during transit to prevent any leakage or safety risks.
    Storage 2-(Prop - 2 - yn - 1 - ylsulfanyl)-1,3 - benzothiazole should be stored in a cool, dry, well - ventilated area away from sources of heat, ignition, and incompatible substances. Keep it in a tightly closed container to prevent exposure to air and moisture. Store it separately from oxidizing agents and acids to avoid potential reactions.
    Application of 2-(Prop-2-Yn-1-Ylsulfanyl)-1,3-Benzothiazole

    In a typical silica-reinforced SBR/BR passenger tire tread formulation processed on an intermeshing twin-screw extruder (L/D 48:1) with discharge temperature maintained at 145–155°C, the introduction of 0.2–1.0 phr 2-(prop-2-yn-1-ylsulfanyl)-1,3-benzothiazole functions as a premature vulcanization inhibitor that does not rely on amine-based retarder chemistry. The compound extends Mooney scorch time (t5, 135°C, per ASTM D1646-19) by 40–120% when assessed against a reference system accelerated exclusively with N-cyclohexyl-2-benzothiazolesulfenamide (CBS), while the subsequent cure rate (t90) measured on a moving die rheometer (ISO 6502:2021) at 160°C deviates by less than 8%, indicating negligible impact on press cycle time. Formulations must comply with EU 1907/2006 (REACH) Annex XVII entries 50–52 concerning PAH migration and with EU 2019/1691 regarding labeling of rubber granules; the additive itself is pre-dispersed in a low-melt EVA binder (MI 4–6 g/10 min) to a 75% active masterbatch before being fed into the first Banbury pass. Four-stage mixing—masterbatch incorporation at 40–60°C, silica-silane coupling at 140–150°C, finalization on an open two-roll mill at 60–70°C, and strip-cooling on a batch-off system—yields a tread compound destined for ECE R30-certified highway tires. The elevated scorch safety margin eliminates the requirement for N-(cyclohexylthio)phthalimide (CTP)-type retarders, thus preserving the integrity of the bifunctional organosilane coupling agent and minimizing ethanol emission during mixing.

    What Regulates the Deep-Section Cure Profile in Insulating Glass Polysulfide Sealants?

    When mixed into a two-component polysulfide liquid polymer (Thiokol™ LP‑32 equivalent) at 0.5–1.5 phr relative to polymer weight, 2-(prop-2-yn-1-ylsulfanyl)-1,3-benzothiazole acts as a latent crosslinking modulator that shifts the gel point without accelerating surface skinning. Dispersion is achieved by pre-blending with the calcium peroxide‑based curing paste in a planetary mixer operated at 25–35 rpm under vacuum (−0.09 MPa) to avoid occluded air, after which the A/B components are metered through a static mixer at a 10:1 volume ratio. Deep-section cure uniformity is assessed by extruding a 12 × 12 × 50 mm ribbon into a 23°C/50% RH chamber and measuring Shore A hardness evolution (ISO 868:2003) at 4 mm and 24 mm depths after 72 h; differential hardness is maintained below 6 points when the alkynyl sulfide is present, compared to 14–18 points in unmodified controls. The sealant must satisfy EN 1279-4:2018 for insulating glass units—notably the moisture penetration index and volatile fogging requirements of Annex E—and retains adhesion to float glass primed with a silane wash after 1 000 h UV irradiation (ISO 11431:2002, method A). Finished products applied in structural glazing and curtain wall assemblies benefit from the extended working life (≥45 min at 23°C) that the additive affords during large-panel installation.

    Heat-Resistant Chloroprene Belting Compounds and Scorch Safety Margins

    Chloroprene (CR) compounds used in multi-ribbed V-belts are processed on a 4-roll inverted L calender at 70–90°C, a temperature window that frequently approaches the critical scorch threshold of ethylene thiourea (ETU)-accelerated systems. Incorporating 0.3–0.8 phr of the benzothiazole alkynyl sulfide expands the processing safety margin by 8–15 min at 120°C (Mooney t10, ASTM D1646-19) while allowing the compound to maintain a minimum crosslink density of 1.8×10⁻⁴ mol/cm³ after press curing at 160°C for 20 min, as verified by equilibrium swelling in methyl ethyl ketone (ISO 1817:2015). The formulation’s compliance is anchored to DIN 22102-1:2014 and ISO 14890:2013 for conveyor belts used in abrasive environments; accelerated heat aging (7 d at 125°C, ISO 188:2023) must not reduce tensile strength retention below 75%. During production, the pre-weighed additive is introduced as a predispersed powder alongside zinc oxide and stearic acid in a tangential internal mixer, dumped at 110–120°C, and sheeted on an open mill before being calendered onto a polyester tension cord. The resultant endless belts find end use in industrial power transmission drives where hot-oil resistance and crack initiation resistance (De Mattia method, ISO 132:2017) beyond 300 kilocycles are mandatory.

    When Sulfur-Donor Cure Systems Encounter Hot Air Aging in Curing Bladder Compounds

    Manufacturing curing bladders from isobutylene-isoprene rubber (IIR) requires a tight crosslink network stable against reversion during 200–220°C cyclic exposure inside a tire press. Addition of 1.0–2.0 phr of the alkynyl sulfide into a resol-cured or alkylphenol disulfide‑cured IIR compound modifies the ratio of mono‑ to polysulfidic crosslinks, as deduced from chemical probe analysis with propane-2-thiol/piperidine (ASTM D7001-20). The modified network exhibits a ≤5% loss in elongation at break after 72 h air aging at 200°C (ASTM D573-04(2019), cell oven method), compared to 12–17% for unblended controls. Processing takes place on a cold-feed vented extruder (90 mm screw, L/D 14:1) delivering a profiled tube to a bladder press capable of 30 MPa clamp force; the compound’s injection temperature is held at 100–105°C to prevent scorch in the runner system. Compliance with FDA 21 CFR 177.2600 for rubber articles intended for repeated food contact must be verified for bladders used in food-grade tire applications (e.g., cargo truck tires carrying edible liquids), and migration limits of ≤0.5 mg/in² in heptane extractives (FDA Guidance for Industry, 2006) are applied. Finished bladders are produced in sizes ranging from 20 to 30 inches bead diameter and deliver extended service lifetimes through minimized oxidative chain scission at the curing interface.

    Steel cord adhesion in heavy-duty radial tire belt skim compounds historically relies on cobalt carboxylate systems that are under increasing scrutiny owing to EU 520/2011 restrictions on soluble cobalt salts. Substitution of 0.5–1.5 phr of 2-(prop-2-yn-1-ylsulfanyl)-1,3-benzothiazole in combination with a reduced cobalt level (0.3 phr cobalt vs. typical 1.0 phr) has been evaluated in a standard sulfenamide‑accelerated NR carcass formulation with a sulfur loading of 3.5 phr. Adhesion is measured on brass-plated (63.5% Cu, 36.5% Zn) steel cord extracted from a 2+2×0.25 mm construction after vulcanization at 150°C for 45 min: the pull-out force (ASTM D2229-23, method B) retains ≥90% of the reference value, while the appearance of the rubber coverage rating (visual assessment, 0–100%) stays above 80%. Critical process parameter is the precise control of compound moisture content below 0.15% before calendering, as the alkynyl group is sensitive to hydrolysis in the presence of residual amines; therefore, a dehumidified feed hopper (dew point ≤ −40°C) is integrated upstream of the four-roll calender. The skim-coated wire is used in truck and bus radial tire belt layers that conform to IATF 16949:2016 manufacturing quality requirements and must survive the ECE R54 endurance test.

    The Compound Acts as a Migration-Resistant Crosslink Modifier in NR/BR-Based Engine Mounts

    Hydraulic engine mounts molded from a natural rubber/butadiene rubber blend (70/30 phr) require dynamic stiffness stability across a −30°C to +80°C service range, a property compromised by slow crystallization of paraffinic waxes and progressive crosslink shortening. Incorporating 0.7–1.3 phr of the alkynyl sulfide into a conventional EV cure system (sulfur 0.8 phr, accelerator 3.5 phr) reduces the Payne effect magnitude (ΔG′, 0.1–15% strain) by 22–28% when measured on an RPA 2000 (ASTM D8059-19) after 500 000 fatigue cycles under fully reversed shear (ISO 4666-4:2018). The additive is introduced during the second Banbury stage at 60–65°C to avoid premature reaction with zinc oxide, and the final compound is injection-molded into the mount carrier with a clamp force of 2 500 kN, a barrel temperature profile of 70–85–90°C, and an injection speed of 35 cm³/s. Conformity to ISO 10846-2:2008 for acoustic testing of resilient elements is documented over the frequency range 1–200 Hz, and the volume swell in IRM 903 oil (70 h at 100°C) is held below 45% as per ASTM D471-16a. The end components, installed in passenger vehicles, must also satisfy OEM specifications for passive road-load durability exceeding 2 million kilometers through salt-spray and ozone-resistance validation.

    Table 1 — Regulatory and Testing Standards Matrix by Application
    Application ContextKey Regulatory/Quality StandardTypical Test Method
    Silica-filled SBR/BR passenger tire treadEU 1907/2006 REACH, ECE R30ISO 6502:2021 (cure rheometer), ASTM D1646-19 (Mooney scorch)
    Two-component insulating glass polysulfide sealantEN 1279-4:2018, Directive 89/106/EECISO 868:2003 (Shore A), ISO 11431:2002 (adhesion after UV)
    Chloroprene multi-ribbed beltingDIN 22102-1:2014, ISO 14890:2013ISO 188:2023 (heat aging), ISO 1817:2015 (swelling)
    IIR curing bladderFDA 21 CFR 177.2600, EU 1935/2004ASTM D573-04(2019) (air oven aging), ASTM D7001-20 (crosslink type)
    Steel cord skim (low-cobalt NR)IATF 16949:2016, EU 520/2011ASTM D2229-23 (wire adhesion), ASTM D471-16a (fluid resistance)
    NR/BR hydraulic engine mountISO 10846-2:2008, SAE J1085ASTM D8059-19 (Payne effect), ISO 4666-4:2018 (fatigue)
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    Certification & Compliance
    More Introduction

    2-(Prop-2-Yn-1-Ylsulfanyl)-1,3-Benzothiazole

    CAS 42293-76-4, molecular formula C10H7NS2, molecular weight 205.30 g·mol⁻¹. This heterocyclic thioether, classified as a substituted 2-mercaptobenzothiazole, is supplied commercially as a crystalline solid of 98 % purity (GC, area normalization) under product codes such as BZT-ALK-98 or PG-BT-S. The compound melts in the range 65–68 °C and exhibits a density of approximately 1.32 g·cm⁻³ at 20 °C. Its solubility profile reveals high affinity for aprotic organic media—solubility in tetrahydrofuran exceeding 250 g·L⁻¹ at 25 °C—while aqueous solubility remains below 0.08 g·L⁻¹, a partition that dictates downstream solvent selection in both formulation and synthesis. Direct application of heat or prolonged storage above 40 °C in the presence of air leads to gradual discoloration and the formation of sulfoxide by‑products (detectable by HPLC at relative retention time 1.35). Consequently, the material is packaged under argon in aluminium‑laminated foil bags and should be re‑sealed under inert gas after each use. Moisture absorption is not thermodynamically favoured; however, pre‑drying over silica gel for 4 h at 30 °C is recommended when ambient relative humidity exceeds 75 %, primarily to prevent agglomeration during precision dispensing in masterbatch preparation.

    Propargyl Substitution Extends Processing Safety without Sacrificing Crosslink Density

    In sulfur‑vulcanised natural rubber (NR) and styrene‑butadiene rubber (SBR) compounds, the substitution of the mercapto proton of 2‑mercaptobenzothiazole (MBT) with a propargyl group fundamentally alters the accelerator’s reactivity profile. Data generated on a 1.8‑L internal mixer (Werner & Pfleiderer GK 1.5E, intermeshing rotors, fill factor 0.72, dump temperature 125–135 °C) and subsequently monitored with an MDR 2000 rheometer (0.5° arc, 160 °C, ASTM D5289-17) indicate that at equimolar sulfur loading (2.0 phr sulfur, 0.8 phr accelerator in an NR/BR 70/30 blend), the scorch time ts2 extends by 35–45 % relative to MBT, while the cure rate index (CRI, defined as 100/(t90 – ts2)) drops from 8.5 min⁻¹ to 6.2 min⁻¹. Despite this delayed onset of crosslinking, the maximum torque (MH – ML) remains within 94 % of the MBT reference, and tensile strength (ASTM D412-16, die C) recorded on a Zwick Z010 universal tester after press‑curing at 150 °C for t90 returns values of 24.1 MPa versus 24.9 MPa for the MBT control. This behaviour is attributed to the thioether linkage stabilising the benzothiazole‑sulfur complex and slowing the release of active sulfurating species; the terminal alkyne remains largely inert under these curing conditions, as confirmed by Raman spectroscopy showing the ν(C≡C) band at 2120 cm⁻¹ persisting in the vulcanizate. The practical ramification on the shop floor is a wider processing window. Injection moulding trials conducted with a 180‑tonne clamp force machine (Engel victory 180, screw L/D 22, melt temperature 95 °C) for a rubber‑to‑metal bonded bushing compound revealed that the compound containing this propargyl derivative tolerated a 12‑second deliberate hold‑time extension without scorch‑induced flow defects, whereas the MBT‑based compound exhibited premature gel particles at the gate after only 7 seconds. This operational latitude translates to reduced scrap rates in multi‑cavity tools where thermal equilibration lag is unavoidable. However, the compound requires 4–6 % higher addition of zinc oxide (ZnO) to fully activate the curative complex, a compensation that can be accommodated within standard 5 phr ZnO formulations without exceeding zinc limits set by certain automotive OEM specifications.

    A Comparative Survey of Benzothiazole Accelerator Architectures

    AcceleratorCASScorch Safety ts2 at 160 °C (min)MH–ML (dN·m)Typical Loading (phr)Distinctive Feature
    MBT (2‑Mercaptobenzothiazole)149-30-41.89.40.6–1.0Rapid cure onset, low cost, limited scorch safety
    MBTS (Dibenzothiazole disulfide)120-78-53.29.10.8–1.2Moderate delay, blooming tendency
    CBS (N‑Cyclohexyl‑2‑benzothiazolesulfenamide)95-33-05.58.70.8–1.5Sulfenamide retarder, amine release
    2‑(Prop‑2‑yn‑1‑ylsulfanyl)‑1,3‑benzothiazole42293-76-42.8–3.48.80.6–1.0Alkyne handle for post‑functionalisation, moderate scorch delay, no free amine

    Rheometer data obtained per ASTM D5289-17 with 0.5° arc, 160 °C, compound base: NR (SMR CV60) 70, BR (Nd‑BR 40) 30, N330 carbon black 45 phr, sulfur 2.0 phr, ZnO 5 phr, stearic acid 2 phr. Values are averages of three independent batches; coefficient of variation does not exceed 6 %.

    The absence of a sulfenamide N–S bond eliminates the risk of amine‑induced nitrosamine formation during curing, a growing concern under European tyre labelling regulations. The alkyne group, while not participating in sulfur crosslinking, provides a covalent anchoring site for subsequent chemical modification—a property absent in all conventional benzothiazole accelerators. This duality positions the compound at the intersection of classical rubber compounding and functional elastomer design. In environments where copper corrosion must be arrested during chemical cleaning, the molecule adopts an entirely different role. The benzothiazole ring adsorbs onto cuprous oxide surfaces through the endocyclic nitrogen and exocyclic sulfur, while the propargyl moiety undergoes chemisorption via the triple bond, forming a polymeric inhibitive film. Electrochemical verification using a standard three‑electrode cell (saturated calomel reference, platinum counter, copper working electrode) in aerated 1.0 M H₂SO₄ at 298 K, per ASTM G59-97 on a Gamry Interface 1010 potentiostat, demonstrated that at a concentration of 1.0 × 10⁻³ M the charge transfer resistance (Rct) extracted from Nyquist plots rose from 140 Ω·cm² (blank) to 3,120 Ω·cm², corresponding to an inhibition efficiency of 95.5 %. Tafel extrapolation gave a corrosion current density of 4.7 µA·cm⁻², compared to 107 µA·cm⁻² for the uninhibited electrolyte. Immersion tests conducted over 168 h in accordance with ASTM G31-21 showed weight‑loss reduction by 92 % at 200 mg·L⁻¹. The inhibitor is particularly effective in the temperature range 30–60 °C; above 70 °C the film begins to desorb, causing a drop in efficiency to 78 %, so its deployment is recommended for pickling baths operating at moderate temperature. Unlike propargyl alcohol, which volatilises and imparts a sharp odour, the benzothiazole derivative has a vapour pressure below 0.01 Pa at 20 °C, significantly reducing toxic inhalatory exposure for line operators. Still, local exhaust ventilation is mandated because the compound is classified as a skin sensitiser (GHS Category 1A) and aquatic chronic category 2 hazard, consistent with other benzothiazoles.

    What Purity Specifications Are Demanded for Copper‑Catalysed Alkyne‑Azide Cycloaddition?

    The terminal alkyne enables Huisgen 1,3‑dipolar cycloaddition with azides under copper(I) catalysis (CuAAC). For this application, purity must exceed 99 % (HPLC, 254 nm) to avoid side reactions from MBT impurities (frequently present at 0.3–0.8 % in the 98 % grade), which can poison the copper catalyst and lead to incomplete conversion. A product specification designed for bioconjugation labelling therefore includes a dedicated assay by quantitative ¹H NMR integrating the acetylenic proton at δ 2.25 ppm (CDCl₃) against an internal standard, with an acceptance criterion of ≥ 99.0 %. Metal content is controlled to < 10 ppm Fe, < 5 ppm Cu, and < 2 ppm Pd to prevent unintended cyclisation prior to use. In a typical reaction with benzyl azide (1.0 eq), CuSO₄·5 H₂O (5 mol%), sodium ascorbate (10 mol%), in H₂O/t‑BuOH (1:1) at ambient temperature, the triazole product forms in 95 % isolated yield after 2 h. The reaction has been successfully scaled to 500 g in a jacketed glass reactor with overhead stirring, with no exotherm detected beyond 2 °C from baseline, rendering the process amenable to kilo‑lab synthesis without specialised calorimetry. Because the benzothiazole ring exhibits a fluorescence quantum yield of 0.04 in the triazole conjugate (excitation 310 nm), the derivative is used to introduce a spectroscopic label into polymers and bioconjugates. The thioether bridge, however, imposes a stability limitation: the conjugate must be shielded from direct UV‑B radiation (280–315 nm) during long‑term storage to prevent photolytic C–S bond cleavage. Dark storage at 4 °C under argon is therefore stipulated; under these conditions, less than 2 % decomposition is observed over 12 months by HPLC.
    Standard / RegulationScopeStatus / Compliance Threshold
    REACH (EC) 1907/2006Registration, Evaluation, AuthorisationPre‑registered; >1 t/a requires full dossier with exposure scenarios
    TSCA (15 U.S.C. §2601)Chemical Substance InventoryListed on Inventory; PMN required for new uses
    IEC 62321‑7‑2:2017Determination of restricted substancesNot directly restricted; benzothiazole content must be declared if >0.1 % w/w in consumer articles per REACH Annex XVII
    FDA 21 CFR 175.300Resinous and polymeric coatings for food contactNot presently listed; extractive testing mandatory for incidental food contact
    GHS Classification (EC) 1272/2008Harmonised hazard communicationSkin Sens. 1A (H317), Aquatic Chronic 2 (H411)
    Storage incompatibilities merit explicit enumeration. Contact with concentrated nitric acid or peroxides leads to rapid exothermic decomposition and formation of benzothiazole sulfonic acids; any cleaning or reaction quenching operations must avoid these oxidants. The compound also reacts vigorously with sodium hydride or organolithium reagents at the acetylenic C–H, generating acetylides that can initiate polymerisation if not properly solvated—a consideration when employing the alkyne in deprotonative metalation sequences. When designing masterbatches for rubber, the accelerator must not be pre‑blended with elemental sulfur and MBTS in the absence of ZnO, because the combination produces a metastable complex that self‑heats and can clump inside silos, blocking pneumatic conveyance lines (25 mm diameter tubing affected in one documented site incident). Instead, a split addition protocol with ZnO added in the first mixing pass and the accelerator with sulfur in the second pass is employed. The product is shipped in fibre drums with polyethylene liners, net weight 25 kg, labelled with GHS pictograms GHS07 (exclamation mark) and GHS09 (environment). A Safety Data Sheet dated to the latest revision of Regulation (EC) No 2020/878 should accompany every consignment. Because an official occupational exposure limit has not been promulgated, a derived no‑effect level (DNEL) of 1.5 mg·m⁻³ for inhalation and 0.2 mg·kg⁻¹ bw·day⁻¹ for dermal exposure is applied based on read‑across from 2‑mercaptobenzothiazole data, as recommended by ECHA’s guidance R.8. Shop‑floor air monitoring using OSHA Method 96 with HPLC‑UV detection allows quantification down to 0.02 mg·m⁻³. Over six months of continuous monitoring at a compounding plant with a usage rate of 80 kg·week⁻¹, all personal breathing zone samples returned values below the analytical limit of detection, provided that weigh‑up operations were conducted inside a downdraft booth with a face velocity of 0.5 m·s⁻¹.