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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 | 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. |
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 IssueHigh-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 WastewaterEffluent 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.
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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| Parameter | Specification | Test 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 ppm | ICP-OES after microwave digestion |
| pH (1% aqueous suspension) | 2.0 – 3.0 | Potentiometric, 25 °C |
| Property | 2-Benzothiazolesulfinic acid | 2-Mercaptobenzothiazole | 2-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 > 200 | 0.12 | > 500 |
| Primary industrial application | Sulfonamide pharmaceutical intermediate, photographic antioxidant | Vulcanisation accelerator, corrosion inhibitor | Electroplating brightener, acid catalyst |
| Key incompatibility | Moisture at pH < 5 leads to rapid disproportionation | Strong oxidisers, metals under heat | Sensitive amines may form genotoxic sulfonate esters |