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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 | 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. |
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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 MarginsChloroprene (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 CompoundsManufacturing 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 MountsHydraulic 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.
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| Accelerator | CAS | Scorch Safety ts2 at 160 °C (min) | MH–ML (dN·m) | Typical Loading (phr) | Distinctive Feature |
|---|---|---|---|---|---|
| MBT (2‑Mercaptobenzothiazole) | 149-30-4 | 1.8 | 9.4 | 0.6–1.0 | Rapid cure onset, low cost, limited scorch safety |
| MBTS (Dibenzothiazole disulfide) | 120-78-5 | 3.2 | 9.1 | 0.8–1.2 | Moderate delay, blooming tendency |
| CBS (N‑Cyclohexyl‑2‑benzothiazolesulfenamide) | 95-33-0 | 5.5 | 8.7 | 0.8–1.5 | Sulfenamide retarder, amine release |
| 2‑(Prop‑2‑yn‑1‑ylsulfanyl)‑1,3‑benzothiazole | 42293-76-4 | 2.8–3.4 | 8.8 | 0.6–1.0 | Alkyne 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.| Standard / Regulation | Scope | Status / Compliance Threshold |
|---|---|---|
| REACH (EC) 1907/2006 | Registration, Evaluation, Authorisation | Pre‑registered; >1 t/a requires full dossier with exposure scenarios |
| TSCA (15 U.S.C. §2601) | Chemical Substance Inventory | Listed on Inventory; PMN required for new uses |
| IEC 62321‑7‑2:2017 | Determination of restricted substances | Not directly restricted; benzothiazole content must be declared if >0.1 % w/w in consumer articles per REACH Annex XVII |
| FDA 21 CFR 175.300 | Resinous and polymeric coatings for food contact | Not presently listed; extractive testing mandatory for incidental food contact |
| GHS Classification (EC) 1272/2008 | Harmonised hazard communication | Skin Sens. 1A (H317), Aquatic Chronic 2 (H411) |