2-Benzothiazolesulfinic Acid, Sodium Salt (1:1)

2-Benzothiazolesulfinic Acid, Sodium Salt (1:1)


    • Product Name 2-Benzothiazolesulfinic Acid, Sodium Salt (1:1)
    • Alias SBBT
    • Einecs 242-856-8
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
    VTB
    Specifications

    HS Code

    248887

    Chemical Formula C7H4NNaO2S2
    Appearance usually white to off - white powder
    Solubility soluble in water
    Melting Point decomposes before melting
    Ph Of Aqueous Solution alkaline
    Odor odorless or very faint odor
    Stability stable under normal conditions
    Hazard Class non - explosive, non - flammable
    Storage Conditions store in a cool, dry place

    As an accredited 2-Benzothiazolesulfinic Acid, Sodium Salt (1:1) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 2 - Benzothiazolesulfinic Acid, Sodium Salt (1:1) in sealed chemical - grade packaging.
    Shipping 2 - Benzothiazolesulfinic Acid, Sodium Salt (1:1) is shipped with strict adherence to chemical transportation regulations. Packed securely in appropriate containers, it's transported by methods ensuring safety and preventing any spillage or damage during transit.
    Storage Store 2-Benzothiazolesulfinic Acid, Sodium Salt (1:1) in a cool, dry place away from heat and direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and contact with air, which could potentially lead to decomposition. Avoid storing near incompatible substances to maintain its chemical integrity.
    Application of 2-Benzothiazolesulfinic Acid, Sodium Salt (1:1)

    In the production of 2-benzothiazolyl sulfenamide accelerators—specifically N-cyclohexyl-2-benzothiazolesulfenamide (CBS, CAS 95-33-0) and N-tert-butyl-2-benzothiazolesulfenamide (TBBS, CAS 95-31-8)—sodium 2-benzothiazolesulfinate functions as the electrophilic sulfur carrier that reacts with the primary amine in an oxidative condensation step. The sodium salt is typically charged as a 30–35 wt% aqueous solution into a jacketed stainless steel or glass-lined batch reactor (common sizes 8–16 m³) equipped with a high-shear turbine agitator operating at 180–240 rpm. Cyclohexylamine or tert-butylamine is introduced at a molar ratio of 1.05:1.0 to 1.12:1.0 relative to the sulfinate to ensure complete consumption of the sulfur carrier while suppressing dialkylamine formation. Sodium hypochlorite solution (12–14% active chlorine, determined per ISO 7393-2) is then metered at a controlled rate of 0.3–0.5 L/min per 1,000 L reaction volume while the batch temperature is maintained at −2°C to +2°C using a chilled brine circulating loop operating at −15°C. The pH is continuously monitored with a glass electrode (Ingold type) and automatically adjusted to 9.5–10.5 by metered 30 wt% sodium hydroxide addition; excursions above 11.0 initiate premature sulfonamide hydrolysis detectable as a 0.8–1.2% rise in free amine, while drops below 8.8 trigger rapid disulfide formation—the resulting 2,2'-dibenzothiazole disulfide (MBTS) is insoluble and increases the filtered product's insolubles by 0.2–0.5%, failing the finished accelerator specification of ≤0.15% ash after sulfated ash determination per ASTM D4574-06. Upon completion of the hypochlorite feed (endpoint detected by starch–iodide paper or online ORP probe at +480 mV ± 20 mV), the crude slurry is cooled to 5°C, discharged into a pressure Nutsche filter, washed with deionized water of conductivity ≤10 µS/cm, and dried in a conical vacuum dryer at 45–55°C under 40 mbar absolute pressure to a moisture content of ≤0.30 wt%. A typical 10 m³ batch yields 900–1,100 kg of CBS or TBBS with an HPLC purity (Agilent 1260 Infinity, C18 column, UV 280 nm) exceeding 99.0%. The dry product is classified under EU REACH (EC No 1907/2006) and, when used as a rubber compounding ingredient, typically complies with rubbers intended for repeated food-contact use under FDA 21 CFR 177.2600 (Category A–C) provided the final vulcanizate passes total migration testing according to EN 1186-1. The commodity grades of CBS and TBBS manufactured via this route are incorporated into the tread compounds of radial truck and bus tires, steel-cord conveyor belts fabricated to DIN 22102, and engine mount compounds where the delayed-action vulcanization profile is critical to processing safety in injection molding at clamp forces above 20,000 kN.

    Parameter CBS Specification TBBS Specification
    Amine:sulfinate molar ratio 1.06–1.10 1.08–1.12
    NaOCl addition temperature 0 ± 2°C −2 to +1°C
    pH control range 9.8–10.4 9.5–10.2
    Drying temperature (°C) 48–52 45–48
    Final product m.p. (DSC, ASTM E794) 97–101°C 104–108°C
    Max. insolubles (% in toluene) 0.10 0.15

    At what dosage does direct addition of the salt suppress premature vulcanization in NR/BR silica-loaded stocks?

    When compounded directly into a natural rubber/butadiene rubber (70/30) silica-filled compound as a scorch retarder, sodium 2-benzothiazolesulfinate is dry-blended into the masterbatch at levels between 0.15 and 0.40 phr. Mixing is performed in an intermeshing tangential internal mixer (e.g., Farrel Banbury F270, fill factor 0.75, ram pressure 0.6 MPa) following a two-stage protocol: in the first non-productive stage, the NR/BR pre-masticated blend, precipitated silica (BET 175 m²/g), silane coupling agent TESPT (8% on silica), ZnO 3 phr, stearic acid 1 phr, and the sulfinate are charged simultaneously and ram-mixed to a drop temperature of 150–155°C; after sheeting off and cooling to 40°C, the productive stage incorporates sulfur 1.6 phr and the primary accelerator CBS at 1.2 phr on a two-roll mill (nip gap 0.8 mm). Mooney scorch measurements at 127°C following ASTM D1646 on a MonTech MV 3000 viscometer reveal a concentration-dependent increase in t5: from 8.2 minutes (0 phr) to 11.5 minutes (0.25 phr) and 14.8 minutes (0.40 phr). Vulcanization rheometry (MDR, ASTM D5289, 160°C/30 min) shows a proportionate delay in t90, exceeding 18 minutes at 0.35 phr, while the maximum torque drop indicates a 7–12% decrease in crosslink density. Tensile properties measured per ASTM D412 using a ZwickRoell Z010 universal tester indicate that at dosages above 0.30 phr the 300% modulus declines by 10–15% relative to the sulfur-only reference, placing a practical upper boundary for the silica-loaded passenger car tire tread formulation. The vulcanizate is intended for low rolling-resistance tire treads and must simultaneously comply with the PAH content limits of EU 1272/2013 (entry 50, Annex XVII of REACH) and the German GS Mark specification AfPS GS 2019:01 PAK. Below 0.15 phr the scorch-protective effect is not statistically distinguishable from baseline, and above 0.45 phr the cure retardation extends processing times beyond the standard press cycle of 12–15 minutes, rendering it uneconomical on multi-cavity curing presses (PIC press, 20-station).

    Sulfinate dosage (phr) Mooney t5 @127°C (min) t90 @160°C (min) 300% Modulus (MPa) Tensile strength (MPa)
    0 8.0 10.2 14.6 24.1
    0.15 9.8 11.6 14.2 23.8
    0.25 11.5 13.3 13.1 22.7
    0.35 13.6 15.8 12.0 21.0
    0.45 16.0 19.5 10.3 18.6

    Substitution of thiuram- and dithiocarbamate-based ultra-accelerators with sodium 2-benzothiazolesulfinate in combination with 2-mercaptobenzothiazole (MBT) has been evaluated in dense and sponge EPDM profiles for nitrosamine-free extrusion curing. The pair exploits the sulfinate’s thermally triggered disproportionation at 140–180°C to release sulfur-active benzothiazole monosulfide species without forming the secondary amine intermediates that produce carcinogenic N-nitrosamines during continuous vulcanization at line speeds exceeding 35 m/min. A representative EPDM formulation contains 100 phr ethylene–propylene–diene terpolymer (ENB-type, ML 1+4 at 125°C = 65), carbon black N550 120 phr, paraffinic oil 90 phr, ZnO 5 phr, stearic acid 1 phr, sulfur 2.0 phr, MBT 1.6 phr, and sodium 2-benzothiazolesulfinate 0.9 phr (pre-dried at 50°C for 2 hours if exposed to RH > 65% to prevent lump formation). Compounding is performed on a cold-feed vented extruder (L/D 20:1, screw diameter 90 mm, temperature zones 40/50/60/65°C from feed to head) followed by a 230°C hot-air curing channel and a microwave vulcanization unit (UHF, 2.45 GHz) powered to achieve a final profile surface temperature of 210°C. The continuous cure is completed within 90–110 seconds, yielding a sponge density of 0.55–0.65 g/cm³ and a dense-skin thickness of 0.3–0.5 mm. Physical testing per ISO 37:2017 (dumbbell die C) shows a tensile strength ≥9 MPa and elongation at break ≥350%; compression set measured per ISO 815-1 (method B, 70°C/24 h) remains below 35%. The vulcanizate is compliant with the German TRGS 552 regulation on workplace N-nitrosamine emissions and with the former EU Directive 93/11/EEC, which limits the migration of N-nitrosatable substances from elastomers for food-contact and toy applications. The extruded components find application in automotive weatherstrips (tested to SAE J2236), building EPDM gaskets for curtain wall joints, and appliance sealing profiles. A critical operational constraint is the reactivity of MBT with zinc oxide at mixing temperatures above 130°C; incorporating the sulfinate too early in the mixing cycle can cause premature activation and scorch in the extruder head, necessitating strict adherence to a 115°C maximum dump temperature in the twin-roll mill homogenization step that precedes extrusion. Published long-term heat-aging data (ISO 188, 120°C/70 h) for this specific accelerator combination is limited, and retention of tensile properties beyond 500 hours at 100°C has not been validated across all EPDM grades, requiring application-specific oven-aging trials before specification freeze.

    An Intermediate for Electroless Nickel Bath Additives: The Sulfinate-Reduction Route to Aromatic Disulfides

    Sodium 2-benzothiazolesulfinate serves as a precursor for synthesizing 2,2'-dithiobis(benzothiazole) (MBTS), a historically established stabilizer and brightness enhancer in acidic hypophosphite-based electroless nickel plating baths. In a typical preparation, the sodium sulfinate is dissolved in deionized water to a concentration of 10–15 wt% and acidified with 98% sulfuric acid to pH 2.0–2.5, then treated dropwise with 30 wt% hydrogen peroxide (stoichiometric excess 5%) at 40–45°C under nitrogen sparging; after 2 hours, the precipitated disulfide is filtered, washed with methanol, and vacuum-dried at 50°C to a purity of ≥97% (GC-MS). The resulting MBTS is formulated into a proprietary liquid additive package at 0.5–1.2 g/L MBTS equivalent and dosed into the electroless nickel bath operating at a temperature of 88–92°C, pH 4.6–5.0, with sodium hypophosphite as the reducing agent. The additive suppresses spontaneous bath decomposition on heated tank surfaces, extends the bath's metal turnover (MTO) from 5 to 8 cycles, and refines the deposit's columnar microstructure to yield an elongation at break of 1.5–2.0% when tested per ISO 4516:2002—a requirement for plated electronic connectors subjected to crimping. Conformance of the plated component is verified against ISO 4527:2003 (electroless Ni-P coatings) and the global RoHS Directive 2011/65/EU for restricted substances. Due to the sensitivity of the hypophosphite bath to organic contamination, the MBTS additive package must demonstrate a TOC surge no greater than 120 mg/L at the working dosage. End products include hard-disk drive actuator arms, L-gauges, and leadframe carriers for semiconductor packaging, where ductile Ni-P films of 8–12 µm thickness ensure reliability during thermal cycling between −65°C and +150°C. Published data for this specific sulfinate-to-disulfide route's impact on phosphorus co-deposition uniformity is limited, and proprietary bath monitoring via continuous spectrophotometric analysis (e.g., Metrohm 2060 Process Analyzer) is recommended to avoid nickel phosphite precipitation when total phosphite exceeds 120 g/L.

    When Benzotriazole Cannot Satisfy REACH Annex XIV Thresholds: 2-Benzothiazolesulfinate as a Building Block for Copper Corrosion Inhibitor Packages

    In water-miscible metalworking fluid (MWF) concentrates designed to replace benzotriazole (BTA) where its potential classification under REACH Annex XIV raises cost and regulatory uncertainty, sodium 2-benzothiazolesulfinate is investigated as a latent precursor that generates the active copper-corrosion-inhibiting species 2-mercaptobenzothiazole (MBT) through alkaline sulfinate reduction. The sulfinate salt is co-neutralized with a long-chain petroleum sulfonate and boric acid ester in the glycol–water carrier of a semisynthetic MWF concentrate, typically at an addition level of 4–6 wt% of the concentrate mass. Upon fluid dilution to a 5% v/v working emulsion in water of hardness up to 400 ppm CaCO₃, the achieved pH of 9.0–9.3 drives the slow conversion of the sulfinate to MBT as verified by reverse-phase HPLC. Corrosion inhibition is evaluated by the ASTM D130-19 copper strip test (3 hours at 100°C), where a dosage delivering 45–55 mg/L of MBT equivalent consistently yields a classification of 1a. The fluid must simultaneously meet the cast-iron chip breakpoint test of ASTM D4627-92 (reapproved 2017) at 7% concentration and demonstrate biological stability via the OECD 301F ready biodegradability test (≥60% degradation within 28 days). On the shop floor, the concentrate is proportioned through a central coolant mixing unit (e.g., Zebra Mix-Master) and delivered to multiaxis CNC lathes machining brass and bronze fittings for potable water systems where nickel release must stay below the 20 µg/L threshold of the EU Drinking Water Directive 2020/2184. A documented incompatibility exists with chlorinated paraffin extreme-pressure additives: batch testing per ISO 9227 neutral salt spray on cast brass panels reveals that sulfinate-generated MBT, when paired with chlorinated paraffins above 2% in the neat phase, can produce yellow-brown staining that downgrades the ASTM D130 rating to 2b, necessitating reformulation with sulfurized fatty esters instead. Published mechanistic data on the sulfinate-to-thiol conversion kinetics in the presence of competing amine corrosion inhibitors in MWF is limited, and formulators must rely on empirical aged-fluid copper coupon immersion tests (internal method, 60°C/500 h) to validate long-term inhibition before field deployment.

    Free Quote

    Competitive 2-Benzothiazolesulfinic Acid, Sodium Salt (1:1) prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please call us at +8615651039172 or mail to sales9@bouling-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615651039172

    Email: sales9@bouling-chem.com

    Get Free Quote of Bouling Chemical Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    The compound designated as 2-Benzothiazolesulfinic Acid, Sodium Salt (1:1) — CAS 2492-23-3, molecular formula C₇H₄NNaO₂S₂, molecular weight 221.23 g·mol⁻¹ — is a heterocyclic sulfinate salt widely utilized as a synthetic intermediate and functional additive. In its anhydrous form, the product appears as a white to off-white crystalline powder with a melting point exceeding 300 °C under decomposition, and exhibits a water solubility of approximately 50 g·L⁻¹ at 25 °C, yielding a mildly alkaline solution (pH 8.0–9.5 at 10 g·L⁻¹). Commercial technical grades are routinely supplied at 97.0% minimum purity (HPLC, λ = 254 nm), with residual sulfite limited to 0.3 wt%, chloride ≤ 0.1 wt%, and heavy metals ≤ 10 ppm as Pb. Unlike the free sulfinic acid, which undergoes rapid disproportionation in air, the sodium salt demonstrates adequate stability under controlled storage (sealed container, ≤ 30 °C, RH < 50%), retaining ≥ 99.5% of original assay over 12 months when protected from moisture.

    What Distinguishes the Sodium Salt from Other Benzothiazole-Sulfur Derivatives?

    A comparison with structurally proximate compounds reveals critical performance differentiators. 2-Mercaptobenzothiazole (MBT, CAS 149-30-4) functions primarily as a primary accelerator in sulfur-cured elastomers, whereas the sulfinate salt serves as a latent vulcanization agent and scorch retarder, decomposing above 140 °C to liberate active sulfur-bearing species without generating 2,2′-dithiobis(benzothiazole) (MBTS) exothermically. Unlike sodium benzothiazole-2-sulfonate, which hydrolytically releases sulfate and impairs vulcanizate aging resistance, the sulfinate anion maintains a S–C bond with higher bond dissociation energy (~ 272 kJ·mol⁻¹) that delays crosslink onset. Differential scanning calorimetry (DSC) of an NBR compound containing 2.0 phr of this sulfinate shows a 12 °C increase in scorch time (ts2 measured per ISO 6502-2:2018) compared to an equivalent loading of sodium p-toluenesulfinate. Additionally, the product exhibits markedly lower migratory aptitude in polyolefin matrices than benzothiazole disulfide derivatives, evaluated via extraction testing according to EN 1186-1:2002, reducing surface bloom in EPDM extrusion profiles.

    Specifications for High-Purity Synthetic Applications

    For pharmaceutical and agrochemical intermediate roles, a refined grade is available conforming to the following profile:

    Refined grade typical batch analysis
    ParameterSpecificationTest Method
    Assay (anhydrous basis)98.5–101.0%Potentiometric titration (NaOH 0.1 M)
    Loss on Drying (105 °C, 2 h)≤ 0.5%Ph. Eur. 2.2.32
    Sulfate (SO₄²⁻)≤ 0.2%Ion chromatography (IC)
    Sulfite (SO₃²⁻)≤ 0.1%Iodometric back-titration
    Residual Solvents (MeOH, EtOH)≤ 500 ppm eachGC headspace, Ph. Eur. 2.4.24
    Iron (Fe)≤ 15 ppmAAS

    The product is classified under REACH registration 01-2119486077-29-0000 and is transported as a non-dangerous good under ADR/RID, provided that packaging meets the moisture-exclusion requirements of UN mark head code 1H2.

    Handling Conditions During Anhydrous Dispersion into Thermoplastic Urethanes

    Processing in TPU extrusion (single-screw, L/D 30:1, compression ratio 3.0:1) mandates pre-drying the powder for 4 h at 60 °C under vacuum (≤ 10 mbar) to achieve residual moisture ≤ 100 ppm. Introducing the sulfinate at a 0.5–1.5 phr loading via a side feeder at zone 4 (barrel temperature 190 °C) prevents premature decomposition. In-situ FTIR monitoring of the melt at the die (ATR probe, diamond crystal) reveals that exceeding a melt residence time of 120 s at 210 °C induces a shoulder at 1045 cm⁻¹ attributable to sulfinate-to-sulfonate oxidation, confirmed by a concomitant rise in melt pressure by 8–10 bar due to microphase separation. Such oxidative byproducts act as chain extenders, raising Shore A hardness by 2–3 points (DIN 53505) and compromising resilience. Thus, compounding with stearically hindered phenolic antioxidants (e.g., Irganox 1010 at 0.2 wt%) is prescribed when line speeds drop below 15 kg·h⁻¹. Conversely, in polyester-TPU shoe sole profiles extruded at high shear (> 2000 s⁻¹), the sulfinate reduces trapped gas pitting, evidenced by 12% fewer surface defects versus formulations using MBTS.

    A nitrile rubber (NBR, 34% ACN) masterbatch formulated in a laboratory internal mixer (Banbury type, 1.6 L chamber, fill factor 0.75) with 2.5 phr of the sodium salt highlights an overlooked rheological conflict. When the dump temperature inadvertently overshoots to 138 °C — only 2 °C above the recommended maximum — cumulative Mooney viscosity (ML 1+4 at 100 °C, ISO 289-1:2015) climbs from 42 MU to 62 MU in subsequent passes. This spike correlates with a 23% reduction in extractable plasticizer (DOP, Soxhlet extraction, ASTM D297), indicating premature grafting. In such borderline-thermal-stability applications, the sulfinate must be pre-blended with a silica carrier (1:1 ratio, Ultrasil VN3) to reduce localized heat accumulation.

    Why the (1:1) Stoichiometry Matters for Aqueous Coupling Reactions

    In palladium-catalyzed desulfinative cross-couplings (Suzuki–Miyaura-type), the precise 1:1 sodium to benzothiazolesulfinate stoichiometry prevents the presence of free acid, which consumes the carbonate base preferentially and degrades the catalytic cycle. When used at 1.2 equivalents relative to an aryl bromide substrate in a dioxane/water (4:1 v/v) mixture with Pd(dppf)Cl₂ (2 mol%), the product yields a coupling efficiency of 89% isolated yield (triphenylene derivative), contrasting with 71% obtained using a technical sulfinate containing 6% free acid impurity. The neutral pH of the sodium salt also obviates the base-induced dehalogenation side reactions observed with potassium 2-thiophenesulfinate at temperatures above 85 °C. Published data for this specific configuration is limited below 0.5 mol% catalyst loading, where competitive protodeborylation becomes non-negligible.

    Electrochemical Bath Composition and Depassivation Behavior

    The product functions as a brightener adjuvant in tin electroplating electrolytes (methanesulfonic acid-based, 180 g·L⁻¹ Sn²⁺, 35 mL·L⁻¹ free MSA). At a bath loading of 0.8–1.2 g·L⁻¹, it raises the cathodic polarization overpotential by 55–70 mV (at 2 A·dm⁻², Hull cell test per DIN 50957), suppressing dendritic growth and yielding a mirror-bright deposit in the 0.5–4.0 A·dm⁻² current density range. The compound’s distinction from commonly employed benzothiazole thioethers lies in its lower vapor pressure and reduced odor, which lowers the required bath ventilation rate (calculated per ACGIH TLV for airborne contaminants). However, continuous bath operation beyond 8 metal turnovers leads to accumulation of sodium formate and benzothiazole, detected by HPLC at 254 nm, which necessitates activated carbon treatment when the total organic carbon exceeds 4.5 g·L⁻¹.

    No single header encompasses the divergent behavior in epoxy resin formulations. When incorporated as a latent accelerator for dicyandiamide-cured (DICY, 6 phr) bisphenol-A epoxy (EEW 190 g·eq⁻¹), 0.3 phr of the sulfinate lowers the onset of cure exotherm from 162 °C to 147 °C (DSC, 10 K·min⁻¹) but raises the glass transition temperature (Tg) of the fully cured network by only 3 °C (DMA, 1 Hz, ASTM D7028). This contrasts sharply with 2-ethyl-4-methylimidazole, which at equivalent weight produces a 12–15 °C Tg depression due to plasticization. Storage stability of a premixed powder coating formulation held at 35 °C for 30 days remains within ± 5% of initial gel time (200 °C, hot plate stroke cure), while the same formulation containing a substituted urea accelerator gels prematurely within 48 h. Adhesion loss on AlMg3 alloy (EN AW-5754) after 500 h salt spray (ISO 9227, NSS) is ≤ 2 mm creep from scribe, meeting the automotive underbody coating criterion of < 3 mm under OEM specification VW TL 260. The product’s divergences from analogous sulfinates become most pronounced under alkaline washing conditions encountered in printed circuit board assembly. When flux residues from a no-clean solder paste (SnAgCu, 96.5/3.0/0.5) are exposed to a 5% sodium carbonate solution at 60 °C, the sulfinate salt present in a conformal coating primer resists hydrolysis, while potassium benzothiazole-2-sulfonate is converted to the 2-hydroxybenzothiazole tautomer, which subsequently corrodes immersion silver finishes (measurable increase in contact resistance from 2.1 mΩ to 18.5 mΩ per IPC-TM-650 2.5.18). This resistance is attributed to the lower electrophilicity of the sulfur atom in the S(O)ONa group versus the SO₃K group, verified by Hammett σp constants derived from 13C NMR shifts.