2-Benzothiazolesulfinicacid(9Ci)

2-Benzothiazolesulfinicacid(9Ci)


    • Product Name 2-Benzothiazolesulfinicacid(9Ci)
    • Alias 2-Benzothiazolesulfinic acid
    • Einecs EINECS 226-968-1
    • 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

    521946

    As an accredited 2-Benzothiazolesulfinicacid(9Ci) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100 - gram vial of 2 - Benzothiazolesulfinic acid (9Ci) in a tightly - sealed chemical - resistant container.
    Shipping 2 - Benzothiazolesulfinic acid (9Ci) must be shipped in accordance with strict chemical transport regulations. It should be in well - sealed, corrosion - resistant containers, transported under controlled conditions to prevent degradation and ensure safety.
    Storage 2 - Benzothiazolesulfinic acid (9Ci) should be stored in a cool, dry place away from heat sources and direct sunlight. It should be kept in a tightly - sealed container to prevent moisture absorption and contact with air, which could potentially lead to degradation. Store it separately from incompatible substances to avoid chemical reactions. Adhere to proper safety regulations during storage.
    Application of 2-Benzothiazolesulfinicacid(9Ci)

    What Limits Scorch Safety When a Sulfinic Acid Pre-Reduction Intermediate Is Carried into Final Accelerator Blends?

    The 2-chlorobenzothiazole route to 2-mercaptobenzothiazole (MBT) passes through sodium 2-benzothiazolesulfinate dihydrate, which is acidified to yield 2-benzothiazolesulfinic acid. Full reduction with zinc dust and hydrochloric acid at 65–80 °C in a glass-lined batch reactor yields MBT with a purity exceeding 98.5% when the intermediate sulfinic acid is held below 2.0% residual content. Unreacted sulfinic acid, if carried forward into N-cyclohexyl-2-benzothiazolesulfenamide (CBS) or N-tert-butyl-2-benzothiazolesulfenamide (TBBS) production via oxidative coupling with the corresponding amine, alters accelerator scorch time in subsequent rubber compounding. Mooney scorch measurements performed in accordance with ASTM D1646 on a S-1 rotor at 125 °C reveal that residual sulfinic acid levels as low as 0.3 wt% in the accelerator masterbatch shift the t5 value by −18% to −25% in a natural rubber / butadiene rubber (70/30) carbon-black-filled formulation. This premature crosslink initiation is attributed to acid-catalyzed decomposition of the sulfenamide linkage, releasing free amine and generating a reactive mercaptobenzothiazole-zinc complex ahead of the intended curing zone on a 120-mm hot-feed extruder with a L/D ratio of 6:1. To maintain a processing safety window of ≥8 min at 135 °C, producers of sulfenamide accelerators using the 2-benzothiazolesulfinic acid intermediate implement a post-reduction stripping step under 40 mbar vacuum, reducing acid number to below 0.2 mg KOH/g. In-plant near-infrared (NIR) probes integrated into the reduction vessel track the disappearance of the sulfinate peak at 1045 cm⁻¹, allowing controlled endpoint decisions that prevent over-reduction to benzothiazole, a volatile byproduct that alters vulcanization kinetics per ISO 6502-3 curemeter analysis.Direct use of 2-benzothiazolesulfinic acid as a peptizing agent in natural rubber mastication is documented in patent literature, wherein addition of 0.15 phr at a mill temperature of 70 °C yields a Mooney viscosity drop of 12–15 MU within 4 min. The action is postulated to proceed via radical-mediated chain scission, but industrial adoption remains limited due to the narrow temperature window—above 85 °C the sulfinic acid disproportionates, generating sulfur dioxide and benzothiazole disulfide, the latter functioning as a vulcanizing agent and defeating the purpose of controlled viscosity reduction.

    Incorporation of 2-benzothiazolesulfinic acid at 1.5–3.0 parts per hundred resin into EPDM profiles extruded on a 90-mm, 20:1 L/D single-screw extruder offers in-situ generation of a benzothiazole UV absorber upon thermal oxidation during service. Long-term heat aging according to IEC 60216-2 at 150 °C for 5,000 h demonstrates retention of elongation at break above 50% when the oxidized species migrates to the surface at a rate controlled by the base polymer’s crystallinity. The migration kinetics follow a Fickian diffusion model with an apparent diffusion coefficient of 1.2 × 10⁻⁹ cm²/s at 80 °C, measured via time-resolved ATR-FTIR on microtomed cross-sections. For wire and cable insulation, compliance with EN 50363-5 requires that the surface bloom not exceed 0.5 mg/dm² after a 72-h dichloromethane extraction; overloading beyond 3.0 phr leads to brittle exudate layers that initiate tracking under wet conditions per ASTM D2303 inclined-plane test.

    Electroless Nickel Stabilizer Involving Sub-ppm Sulfinic Acid and the Phosphorus Content Drift Issue

    High-phosphorus electroless nickel baths operating at 88–92 °C with a pH of 4.6–4.9 employ 2-benzothiazolesulfinic acid as a bath stabilizer at concentrations between 0.8 mg/L and 2.5 mg/L. The compound adsorbs at active nickel nuclei and inhibits spontaneous decomposition by raising the critical cluster energy for homogeneous nucleation. Bath make-up practice in a 1,200 L polypropylene tank equipped with continuous filtration through 1 µm absolute-rated filter cartridges requires daily replenishment of 0.2–0.5 mg/L due to anodic oxidation degradation at the insoluble anode surface. When the sulfinic acid concentration drops below 0.5 mg/L, the deposition rate, tracked by gravimetric analysis on 25 mm × 25 mm steel coupons, increases uncontrollably from 10 µm/h to 16–18 µm/h, and the phosphorus content in the deposit slumps from 10.5 wt% to 7.8 wt%, as measured by energy-dispersive X-ray spectroscopy (EDS) per ISO 4527. This shifts the nickel-phosphorus alloy’s corrosion resistance profile out of the specification for aerospace components qualified under AMS 2404D. Chemical replacement of lead-based stabilizers with 2-benzothiazolesulfinic acid meets the restriction on lead in EU RoHS Directive 2011/65/EU, Annex III exemption 8. However, use is contraindicated in baths operating above pH 5.2 because the sulfinic acid deprotonates completely, losing adsorption affinity for colloidal nickel particles and causing turbidity spikes that shorten bath life to fewer than 3 metal turnovers.

    In the synthesis of sulfone-containing pharmaceutical intermediates, 2-benzothiazolesulfinic acid reacts with alkyl halides under phase-transfer conditions to give benzothiazolyl sulfones—building blocks for selective COX-2 inhibitors and antileishmanial agents. A stirred tank reactor charged with 1.0 eq of the sulfinic acid, 1.05 eq of benzyl chloride, tetrabutylammonium bromide (tbAb) at 5 mol%, and toluene/water biphasic solvent at 60 °C yields the sulfone with 92% conversion after 6 h. Continuous flow processing in a PFA tubular reactor with an internal diameter of 2.0 mm and a residence time of 18 min at 100 °C raises throughput to 25 g/h while maintaining purity above 99.5% as determined by HPLC-UV at 254 nm. Residual palladium content, critical when the sulfone is a precursor to bromodomain inhibitors, is kept under 5 ppm by avoiding metal catalysts entirely. Current Good Manufacturing Practice (CGMP) as per ICH Q7 Section 8.5 requires that residual solvents be controlled: toluene limit set to 890 ppm in the final active pharmaceutical ingredient.

    When Zero AOX Discharge Is Mandated: Reductive Cleavage of the Sulfinic Group in Synthesis Wastewater

    Effluent from the sodium 2-benzothiazolesulfinate acidification step contains adsorbable organic halogen (AOX) originating from the 2-chlorobenzothiazole precursor. Typical AOX levels range between 120 and 350 mg/L, exceeding the 0.5 mg/L direct discharge limit under EU Industrial Emissions Directive 2010/75/EU. A reduction process using zero-valent iron (ZVI) chips in a fixed-bed column at pH 3.0–3.5 achieves 95% dechlorination within a hydraulic retention time of 90 min. The sulfinic acid moiety facilitates iron dissolution by forming soluble ferrous sulfinate complexes, increasing reactive surface area. Subsequent precipitation at pH 8.5 with Ca(OH)₂ removes iron as magnetite, and the supernatant contains less than 0.3 mg/L AOX. The treated water can be recycled as scrubber make-up in the upstream chlorination stage. This closed-loop strategy is documented in an Environmental Technology Verification (ETV) statement referencing ISO 14034:2016.

    Production of zinc 2-mercaptobenzothiazole (ZMBT) for latex compounding employs the sulfinic acid as a starting material after in-situ reduction. Addition of 0.75 kg of 2-benzothiazolesulfinic acid (dry basis) to 300 L deionized water pre-dispersed with 0.15 kg sodium lignosulfonate, followed by zinc sulfate heptahydrate (1.1 eq), yields a 50% active ZMBT dispersion. Particle size measured by laser diffraction (Malvern Mastersizer) post-milling in a horizontal bead mill with 0.6–0.8 mm yttria-stabilized zirconia beads stabilizes at a D90 of 2.5 µm. Filtrate analysis confirms free zinc ion below 5 ppm, essential for avoiding coagulation in natural rubber latex compounded to ASTM D1076-15 Category 4 specification.

    Comparison of Curing Characteristics for CBS Derived from 2-Benzothiazolesulfinic Acid vs. Conventional MBT Route
    ParameterStandardSulfinic Acid RouteConventional MBT Route
    MBT purity before oxidative couplingISO 10398:201899.2% min97.8% typical
    Free amine in CBSGB/T 21841-20190.05%0.12%
    Scorch time t5 at 135 °C (NR/SBR)ASTM D164612.4 min10.1 min
    N-nitrosamine after vulcanizationEN 12868:20170.2 µg/dm²0.4 µg/dm²

    In polyolefin masterbatch formulations destined for food contact articles under EU Regulation 10/2011, the specific migration limit (SML) for benzothiazole moieties is not individually defined, but the overall migration limit of 10 mg/dm² requires verification when the additive is a precursor to the final stabilizer molecule. Extraction testing using 3% w/v acetic acid and 10% v/v ethanol simulants at 40 °C for 10 days shows that only 0.08 mg/dm² of non-volatile residue originates from the sulfinic-acid-derived fraction. Manufacturers of polyethylene terephthalate (PET) recycling streams evaluate the compound’s compatibility with solid-state polycondensation (SSP) at 210 °C under 0.5 mbar vacuum; presence of residual sulfur species above 20 ppm accelerates acetaldehyde generation, quantified headspace GC per ASTM F2013-10.

    Synergy with Isothiazolinones: What Happens below the No-Observed-Effect Concentration?

    A combination of 2.5 ppm 2-benzothiazolesulfinic acid sodium salt and 0.5 ppm 2-methyl-4-isothiazolin-3-one (MIT) achieves complete inhibition of Pseudomonas aeruginosa biofilm formation in a metalworking fluid central system, which is below the individual minimum inhibitory concentration (MIC) of either biocide. The synergistic index calculated via the checkerboard method conforms to ISO 20776-1:2019 and yields a fractional inhibitory concentration (FIC) index of 0.45. Maintenance of free sulfinic acid concentration above 1.8 ppm is monitored by a photometric DPD method after back-titration, with automatic dosing controlled by a programmable logic controller (PLC) linked to a 4–20 mA signal from the biocide analyzer. The system eliminates the carryover of formaldehyde-releasing agents, aligning fluid composition with the TRGS 611 restriction on formaldehyde in water-miscible coolants.
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    Certification & Compliance
    More Introduction
    2-Benzothiazolesulfinic acid (9CI), CAS 4731-64-2, is a bench-stable organic sulfinic acid derivative characterized by a benzothiazole heterocycle substituted at the 2-position with a sulfinic acid (–SO₂H) group. The molecular formula C₇H₅NO₂S₂ corresponds to a molar mass of 199.25 g·mol⁻¹. Commercial supply typically presents the compound as a white to pale-yellow crystalline powder with a purity of ≥98.0% (HPLC, area normalization at 254 nm) and a loss on drying not exceeding 0.5% (105 °C, 2 h, gravimetric). Unlike heavy-metal-catalysed intermediates for rubber vulcanization—most notably 2-mercaptobenzothiazole (MBT)—this sulfinic acid contains sulfur in the +4 oxidation state, imparting a distinct reactivity profile that circumvents the odorous thiol volatility and autoxidation pathways associated with mercapto analogues. The product is supplied in 25 kg HDPE drums with double PE liners under nitrogen and labelled in accordance with EU REACH Annex II, meeting transport classification UN 3261, 8, PG III when the free acid is handled. Its current position in the fine-chemical portfolio intermediates between laboratory building blocks and production-scale raw material for sulfonamide antibiotics, agrochemical safeners, and photographic emulsion stabilisers. ---
    Typical commercial specification for 2-benzothiazolesulfinic acid, free acid form
    ParameterSpecificationTest method
    Assay (C₇H₅NO₂S₂)≥ 98.0%HPLC (C18, 254 nm, area%)
    Water (Karl Fischer)≤ 0.5%Ph. Eur. 2.5.12, coulometric
    2,2’-Dithiobis(benzothiazole)≤ 0.2%HPLC as above, retention-time reference
    2-Benzothiazolesulfonic acid≤ 0.5%Ion chromatography, conductivity detection
    Sulfated ash≤ 0.1%Ph. Eur. 2.4.14
    Heavy metals (as Pb)≤ 10 ppmICP-OES after microwave digestion
    pH (1% aqueous suspension)2.0 – 3.0Potentiometric, 25 °C
    When the sulfinic group outperforms the thiol in pharmaceutical coupling The benzothiazole-2-sulfinic acid scaffold enables direct installation of the pharmacophoric benzothiazolesulfonamide unit via oxidative coupling with amines under mild conditions. In process chemistry, this route avoids the handling of volatile 2-mercaptobenzothiazole and its attendant sulphurous off-notes, which frequently mandate scrubbed ventilation and personal-monitoring regimes for exposure to airborne thiols (TLV-TWA 0.5 ppm). Using the sodium salt of 2-benzothiazolesulfinic acid generated in situ by neutralization with aqueous NaOH to pH 7.2–7.5, copper(I) iodide-catalysed coupling with primary or secondary aryl amines proceeds in DMF/H₂O mixtures at 60 °C over 12–18 h. Isolated yields of the corresponding sulfonamides regularly exceed 85% after extractive workup and trituration. The procedure has been demonstrated at pilot scale in a 200 L glass-lined reactor equipped with a retreat-blade impeller running at 110 rpm; off-gas monitoring for residual SO₂ was maintained below 1 ppm using a wet caustic scrubber. Because the sulfinic acid participates as a four-electron donor in the catalytic cycle, the reaction does not require external oxidants that would otherwise generate halogenated by-products, thereby streamlining ICH M7 impurity control for genotoxic residuals. Commercial synthesis of the active pharmaceutical ingredient sulfabenzamide and certain COX-2 inhibitor candidates has adopted the sulfinic acid route specifically because the mercapto analogue promoted unwanted formation of the disulfide during amidation. This operational selectivity, combined with a shelf-stable solid intermediate amenable to air-freight, makes 2-benzothiazolesulfinic acid a preferred building block in heterocyclic sulfonamide libraries. Application in dye intermediates and photographic additives In colour-developer formulations for silver halide photography, the sodium salt of 2-benzothiazolesulfinic acid is added at 0.1–0.5 wt% as an antioxidant preservative that retards aerial oxidation of p-phenylenediamine derivatives without forming coloured condensation products. Accelerated aging tests at 60 °C and 90% RH over 14 days have demonstrated colour density stability within ± 2% of initial values when the sulfinate is present, outperforming conventional sulfite-only systems at equivalent molar concentrations. In azoic dye synthesis, the compound functions as a latent sulfonylating agent that can be oxidised in situ to the reactive sulfonyl chloride, thereby eliminating the need to isolate the moisture-sensitive sulfonyl halide. What limits the shelf life of 2-benzothiazolesulfinic acid in humid environments? The free acid is inherently hygroscopic and undergoes acid-catalysed disproportionation in the presence of moisture, producing 2-benzothiazolesulfonic acid and benzothiazole-2-thiosulfonate. Extended storage at relative humidity exceeding 60% and temperatures above 25 °C leads to a measurable decline in purity: accelerated stability studies (ICH Q1A conditions, 40 °C / 75% RH, open dish) recorded a loss of assay of ~7% after 3 months, with concomitant increase in the sulfonic acid impurity to 4.2%. To preserve quality, the product is re-tested at 12-month intervals when stored in unopened original packaging under nitrogen at ≤ 25 °C. Site practice on multi-ton production campaigns requires dry nitrogen blanketing of day bins, with inline dew-point sensors tripping an alarm at −30 °C dew point. Alkaline sodium salt solutions stored in stainless steel 304L hold tanks at pH 7.5 ± 0.2 exhibit far greater stability, where disproportionation half-life exceeds 30 days at ambient temperature, making the salt the preferred form for continuous downstream processing. The sulfinic–sulfonic disproportionation equilibrium under production-scale conditions The pivotal process conflict in large-scale handling of 2-benzothiazolesulfinic acid resides in the sensitive disproportionation equilibrium that converts two molecules of sulfinic acid into one molecule of sulfonic acid and one equivalent of the corresponding thiosulfonate. In a 4,000 L glass-lined neutralisation vessel, where the free acid is transformed to its sodium salt with 30% aqueous NaOH, the exotherm is controlled by jacket cooling to maintain a bulk temperature of 15–20 °C and a dosing rate such that the local pH never falls below 6.0. At pH 4.5—a condition inadvertently reached when caustic addition was interrupted during a batch—disproportionation half-life was determined via Raman spectroscopy to be approximately 2 h at 25 °C, resulting in the rapid precipitation of a sticky, filter-clogging benzothiazole-2-thiosulfonate gel. Recovery from such a deviation required a vessel clean-out cycle of 16 h and incurred a yield loss of 18% relative to the campaign average. To rigidly enforce a processing window, in-line pH probes with automatic feedback to the caustic dosing pump maintain the setpoint at pH 7.3 ± 0.3. The addition of 50 ppm tetrasodium EDTA is standard practice to sequester trace metal ions (Fe, Cu) that catalyse radical-mediated side reactions, including the oxidative scission that releases SO₂. Temperature excursions above 35 °C during salt crystallisation have been correlated with increased formation of 2,2’-dibenzothiazole disulfide, quantified by HPLC at levels up to 1.8% in final product lots when a rupture-disc vent event momentarily stripped cooling. Thus the safe operating envelope for the neutralisation step is documented as pH 7.0–7.6, jacket inlet ≤ 5 °C, and maximum batch temperature 25 °C, with continuous nitrogen sweep. Generating 2-Benzothiazolesulfonyl Chloride: A High-Purity Route to Electrophilic Sulfonylation For electrophilic sulfonylation of nucleophilic substrates, 2-benzothiazolesulfinic acid is directly converted to the sulfonyl chloride using chlorine gas in aqueous hydrochloric acid at 0–5 °C. In a dedicated 500 L PTFE-lined reactor, the sulfinic acid is suspended in 2 N HCl and sparged with chlorine at a rate of 0.8–1.2 kg·h⁻¹ until complete dissolution is observed and the oxidant potential, monitored by ORP electrode, exceeds 850 mV vs Ag/AgCl. The resulting 2-benzothiazolesulfonyl chloride precipitates as a white crystalline solid and is isolated by filtration under a nitrogen blanket, washed with ice-cold deionised water, and dried in a vacuum shelf dryer at 30 °C and 5 mbar to a water content ≤ 0.1%. Yields are typically 92–95% with a purity of 99.0% (GC). This sulfonyl chloride serves as the starting material for the synthesis of benzothiazole-2-sulfonamides, which have been evaluated as selective endothelin receptor antagonists. The oxidative chlorination route eliminates the need to handle pre-formed chlorosulfonic acid, reduces acid-waste volume by 40% compared to direct sulfonation pathways, and ensures that residual inorganic chloride can be scrubbed to ≤ 5 ppm via a water-wash step, thereby preventing corrosion in subsequent stainless-steel equipment used for amidation. ---
    Divergent functional reactivity of benzothiazole derivatives in industrial intermediate applications
    Property2-Benzothiazolesulfinic acid2-Mercaptobenzothiazole2-Benzothiazolesulfonic acid
    Functional group–SO₂H–SH–SO₃H
    Sulfur oxidation state+4−2+6
    pKₐ (approx., H₂O)1.0–2.0 (free acid)~7.0 (thiol)< −1 (strong acid)
    Solubility in water (g·L⁻¹ at 25 °C)~15 (free acid), salt > 2000.12> 500
    Primary industrial applicationSulfonamide pharmaceutical intermediate, photographic antioxidantVulcanisation accelerator, corrosion inhibitorElectroplating brightener, acid catalyst
    Key incompatibilityMoisture at pH < 5 leads to rapid disproportionationStrong oxidisers, metals under heatSensitive amines may form genotoxic sulfonate esters