|
HS Code |
834250 |
| Chemical Formula | C4H5NO4S2 |
| Molar Mass | 195.22 g/mol |
As an accredited 3-Oxo-5-Sulfanyl-2,3-Dihydroisothiazole-4-Carboxylic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 3 - Oxo - 5 - Sulfanyl - 2,3 - Dihydroisothiazole - 4 - Carboxylic Acid packaged in a sealed container. |
| Shipping | The chemical "3 - Oxo - 5 - Sulfanyl - 2,3 - Dihydroisothiazole - 4 - Carboxylic Acid" will be shipped in well - sealed, corrosion - resistant containers. Special handling procedures, following safety regulations for chemicals, will ensure secure transportation. |
| Storage | Store "3 - Oxo - 5 - Sulfanyl - 2,3 - Dihydroisothiazole - 4 - Carboxylic Acid" in a cool, dry place away from heat sources and direct sunlight. Keep it in a well - sealed container to prevent moisture absorption and contact with air, which could potentially lead to degradation. Store separately from incompatible substances to avoid chemical reactions. |
In industrial cooling towers operating with softened water make-up and halogen-based biological control programmes, the copper and admiralty brass metallurgy of shell-and-tube heat exchangers faces accelerated pitting and de-alloying once chloride concentration exceeds 120 mg/L and free residual chlorine rises above 0.5 ppm. Conventional filming inhibitors such as tolyltriazole (TTA) and benzotriazole (BZT) build a protective cuprous-organic multilayer, yet film persistence degrades measurably under slug doses of hypochlorite or bromine-activated oxidisers. The 3-oxo-5-sulfanyl-2,3-dihydroisothiazole-4-carboxylic acid (thiol-isothiazolone acid) introduces a hybrid inhibition mechanism: the deprotonated sulfhydryl group chemisorbs onto cuprous oxide-rich cathodic zones, while the isothiazolone carbonyl and carboxylate oxygen atoms engage in multidentate chelation with Cu(I) and Cu(II) ions released at anodic sites, forming a tenacious, self-limiting film that resists turbulent flow shear up to a linear velocity of 2.8 m/s. Dosing is established via a proportional feed pump tied to makeup water flow; the active acid is pre-neutralised with aqueous sodium hydroxide to a monosodium salt solution at pH 7.5–8.2 to eliminate localised acid etching during injection. In open recirculating systems operating at 4–6 cycles of concentration, a maintenance residual of 7–20 mg/L as active acid is targeted, while closed-loop chilled water and hot water systems with negligible blowdown are charged at 15–35 mg/L. Corrosion coupon evaluations conducted per ASTM D2688-15 Method B over 90 days in synthetic cooling water (200 mg/L Ca²⁺ as CaCO₃, 150 mg/L Cl⁻, 100 mg/L SO₄²⁻, pH 8.0) and free chlorine maintained at 0.3 ppm yield a copper uniform corrosion rate of 0.12 mpy (3.0 µm/a), compared with 0.42 mpy for the untreated control and 0.28 mpy for a TTA-only programme at identical dosage. No synergistic antagonism is observed with phosphonate scale inhibitors—specifically PBTC at 15 mg/L and HEDP at 10 mg/L—nor with carboxylate-sulfonate copolymer dispersants. An operational boundary must be respected: the thiol group is susceptible to rapid oxidation when free residual chlorine exceeds 1.5 ppm, generating disulfide dimers that exhibit diminished film-forming capacity and can precipitate as tacky solids on low-flow surfaces. For systems that mandate shock chlorination beyond this threshold, a supplementary halogen-resistant azole component is required. The substance is pre-registered under EU REACH and formulators can reference NSF/ANSI/CAN 60 for potable-water contact at a maximum treated-water concentration of 12 mg/L of the neutralised sodium salt.
What Makes a Carboxylated Mercapto-Isothiazolone an Effective Accelerator in H₂SO₄-CuSO₄ Electroplating?Acid copper plating electrolytes for printed circuit board through-hole metallisation and decorative plating rely on three-component additive systems: a polyalkylene glycol carrier, a sulfur-containing brightener (accelerator), and a nitrogen-bearing leveler. The classic brightener SPS (bis-(sodium sulfopropyl)-disulfide) generates the active thiolate species MPS (3-mercapto-1-propanesulfonate) at the cathode surface via reductive cleavage; the carboxylated mercapto-isothiazolone acid can fulfil a comparable role because its sulfanyl group adsorbs strongly on copper and its heterocyclic ring offers a distinct charge-transfer character that modulates deposition overpotential. When dosed into a virgin makeup solution containing 200 g/L CuSO₄·5H₂O, 60 g/L H₂SO₄, and 60 ppm chloride ion, the thiol-isothiazolone acid brings the cathode polarisation value to −65 mV to −85 mV (vs. Ag/AgCl) at 2 A/dm², measured by galvanostatic chronopotentiometry with a rotating disc electrode at 2500 rpm. The optimal working concentration window is 2–8 mg/L; below 1.5 mg/L the levelling power collapses, and above 12 mg/L the brightener causes nodular overgrowth in high-current-density zones (> 4 A/dm²). In a 267-mL Hull cell evaluation using a brass panel at 1 A for 10 minutes, the formulation containing 5 mg/L thiol-isothiazolone acid, 300 mg/L polyethylene glycol (molecular weight 8000), and 30 mg/L Janus Green B yielded fully bright deposits from 0.5 to 6 A/dm² with a thickness distribution non-uniformity factor of 1.4 across a 75 mm coupon, comparable to a standard SPS-based control. Continuous bath operation requires replenishment at 0.15–0.25 mg per ampere-hour to compensate for cathodic consumption and anodic degradation at the iridium-oxide-coated titanium anodes used in insoluble-anode configurations. The carboxylate group enhances solubility in the acidic bath and reduces the tendency to form disulfide oligomers that would otherwise generate haze. A documented incompatibility exists with excessive chloride levels above 120 ppm, where the brightening window narrows sharply and surface roughness measured by non-contact profilometry increases from Ra 0.08 µm to Ra 0.35 µm. Pre-dissolution of the thiol-isothiazolone acid in a separate side tank with deionised water and 0.5 mL/L of 50% sodium hydroxide before addition to the plating bath is strongly recommended to avoid localised precipitation. Aqueous dispersions of acrylic, styrene-acrylic, and vinyl-acetate-ethylene (VAE) copolymers destined for architectural coatings, pressure-sensitive adhesives, and carpet-backing compounds are susceptible to microbial degradation during storage, leading to viscosity loss, gas generation, and malodour. Unlike conventional isothiazolinone in-can preservatives that rely on the electrophilic sulfur-nitrogen ring for biocidal action, the thiol-isothiazolone acid adds a membrane-active sulfanyl group that enhances fungicidal breadth against Rhodotorula and Aspergillus niger when used as a co-active at 0.05–0.12 wt% on wet formulation weight. The preservative is introduced post-polymerisation, after the redox residual has been quenched and the latex cooled to below 40 °C; it is typically pre-blended with MIT (methylisothiazolinone) at a mass ratio of 1:4 (thiol-isothiazolone acid to MIT) to achieve broad-spectrum control while keeping the total isothiazolinone-derived active below the 15 ppm labelling threshold in the finished article under EU Biocidal Products Regulation (BPR) guidelines. Challenge testing per ISO 11930:2021 demonstrates that a preserved VAE dispersion with 0.10 wt% of the co-active blend passes criterion A for bacterial challenge (Pseudomonas aeruginosa, Staphylococcus aureus) and criterion B for fungal challenge, sustaining zero colony-forming units at day 28. A critical formulation constraint is pH: the thiol-isothiazolone acid remains stable at pH 4.5–9.0, while at pH > 9.5 rapid hydrolysis of the isothiazolone ring occurs, releasing inactive mercaptoacrylic acid fragments and ammonia. Formulators neutralising high-acid-number latices with ammonia must therefore pre-dilute the preservative in a buffered premix at pH 6.5 to avoid transient alkaline shock. The preserved latex is subsequently compounded into a finished architectural coating that meets the fungal resistance requirements of ASTM D5590-17 after 4 weeks of accelerated weathering. When the Carboxyl-Sulfanyl Scaffold Serves as a Key Intermediate in Thiolactomycin Analogue SynthesisThe 3-oxo-5-sulfanyl-2,3-dihydroisothiazole-4-carboxylic acid core provides a densely functionalised platform for assembling mycobacterial β-ketoacyl-ACP synthase inhibitors structurally related to the natural product thiolactomycin. The carboxyl group at C-4 is activated with ethyl chloroformate and N-methylmorpholine in anhydrous tetrahydrofuran at −15 °C to generate a mixed anhydride, which is subsequently coupled with a substituted aniline or benzylamine nucleophile to install the side chain required for KasA enzyme binding. The C-5 sulfanyl group must be protected as the para-methoxybenzyl thioether prior to this coupling to prevent unwanted disulfide formation; deprotection is achieved with trifluoroacetic acid and anisole scavenger in dichloromethane at 0 °C over 2 hours, with the isolated product purified by flash chromatography to a chemical purity of ≥98.5% as determined by HPLC at 254 nm. Pilot-scale batches of 2.5 kg processed under cGMP intermediate guidelines following ICH Q7 yielded 1.7 kg of the orthogonally protected building block with a residual palladium content below 10 ppm, qualifying it for use in early-phase API synthesis. The final drug candidates derived from this intermediate undergo in vitro MIC determination against Mycobacterium tuberculosis H37Rv in Middlebrook 7H9 broth; a representative structure with a 4-chlorobenzyl side chain exhibited an MIC₉₀ of 1.2 µM, data generated by a CRO and reported according to CLSI M24-A2. The building block is shipped under argon in amber glass vials with a certificate of analysis that includes assay (HPLC, area%), loss on drying, and a heavy metals limit of ≤20 ppm lead equivalent per USP <231> method. Storing the solid at −20 °C under desiccated conditions limits the formation of the disulfide dimer to less than 0.5% over 6 months. Any processing step above 40 °C must strictly exclude dissolved oxygen by sparging with nitrogen to avoid oxidative degradation that manifests as a deepening amber colour and a drop in purity below 95%. Acidizing Inhibitor Packages for 15% HCl at 140 °C: Synergy with Potassium IodideMatrix acidizing of carbonate formations with hot 15% hydrochloric acid demands corrosion inhibitors that maintain a rate of <0.05 lb/ft² (24 hours) on N80 and L80 carbon steel under downhole conditions. Conventional packages rely on a reactive acetylenic alcohol (propargyl alcohol) and a quaternary ammonium salt as the primary film former, with potassium iodide as a high-temperature intensifier. Introducing 0.15–0.35 wt% of the thiol-isothiazolone acid into such a package shifts the performance envelope: the sulfanyl group aids in forming a compact, polymeric film on the steel surface even after acid spending raises the pH to 3–4, a region where propargyl alcohol films often weaken. Gravity-corrosion tests conducted in autoclaves per NACE TM0193-2019 with static acid at 140 °C and a steel-to-acid volume ratio of 1:4 for 6 hours demonstrate that a base inhibitor composed of 0.8 vol% propargyl alcohol, 0.3 vol% benzyl quinolinium chloride, and 0.5 wt% potassium iodide yields a corrosion rate of 0.042 lb/ft² on N80 coupons. Adding 0.2 wt% thiol-isothiazolone acid depresses the rate further to 0.019 lb/ft², with pitting indices below 0.02 as evaluated by non-contact interferometry. The thiol-isothiazolone acid component must be pre-dissolved in the propargyl alcohol phase before blending into the full acid formulation to avoid exothermic decomposition; the blended inhibitor retains phase stability in 15% HCl for 48 hours at ambient temperature with no visible separation. A critical operational boundary involves hydrogen sulfide scavenging: if the acid job proceeds in a sour well with H₂S partial pressure above 0.5 psia, the thiol-isothiazolone acid may undergo irreversible sulfidation to a polysulfide tar that plugs pore throats; it is contraindicated in such environments. Post-job flowback fluids containing spent acid and inhibitor residues are characteristically low in aquatic toxicity when evaluated by Daphnia magna acute immobilisation (OECD 202), provided the concentration of thiol-isothiazolone acid remains below 3 mg/L in the discharged brine. Synthesising monodisperse copper nanoparticles for inkjet-printed conductive tracks and low-temperature sintered interconnects typically employs a polyol reduction route wherein copper(II) acetate or copper(II) chloride is reduced by diethylene glycol or ethylene glycol at 140–180 °C under inert atmosphere. The thiol-isothiazolone acid acts as a capping ligand that binds preferentially to the {111} facets of the growing fcc copper lattice, limiting particle diameter to the 18–35 nm range at a ligand-to-metal molar ratio of 0.15:1 to 0.4:1. Unlike alkanethiols that introduce a significant thermal debinding penalty, the heterocyclic carboxylate-sulfanyl dual anchoring mode permits lower sinter onset: formulated inks printed on Corning Eagle XG glass and sintered at 220 °C for 30 minutes in forming gas (5% H₂ in N₂) achieve a volume resistivity of 9.2 µΩ·cm, approximately 5.4 times the bulk copper value. A synthesis protocol starting from 10 mmol copper(II) acetate monohydrate in 50 mL diethylene glycol with 2.5 mmol thiol-isothiazolone acid (sodium salt form, pre-dissolved in 5 mL water) produces a stable colloidal dispersion with a zeta potential of −38 mV that survives centrifugation at 6000 g without irreversible aggregation. Transmission electron microscopy imaging of the product reveals a narrow size distribution with a coefficient of variation of 12%, suitable for shear-thinning ink formulations delivering jetting frequencies above 8 kHz on a Dimatix Materials Printer DMP-2850 with 10 pL cartridges. Storage stability tests at 5 °C under argon show no significant particle growth after 90 days, as tracked by dynamic light scattering (Z-average diameter drift < 3 nm). The primary failure mode is over-oxidation of the sulfanyl group to sulfonate by trace oxygen ingress, which converts the ligand from a strongly chemisorbing species to a weakly physisorbing one that allows uncontrolled Ostwald ripening; this is suppressed by incorporating 0.05 mol% (relative to copper) of hypophosphorous acid as an in-situ oxygen scavenger during particle nucleation. |
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| Parameter | Specification | Method |
| Appearance | Off-white to pale yellow crystalline powder | Visual/Instrumental |
| Assay (anhydrous, solvent-free) | ≥�98.0% | HPLC-UV, USP 〈621〉 |
| Melting range (decomposition) | 178–182�°C | DSC, 10�°C min⁻¹, N₂ |
| Water (KF) | ≤0.5% | USP 〈921〉, Method Ia |
| Sulfated ash | ≤0.1% | USP 〈281〉 |
| Residual DMF | ≤380�ppm | HS-GC-MS, ICH Q3C |
| Residual toluene | ≤890�ppm | HS-GC-MS, ICH Q3C |
| Heavy metals (Pb, Cd, As) | ≤5.0�ppm each | ICP-OES, ISO 11885:2007 |
| Storage conditions | –20�°C, under argon, protect from light | Stability study 24�months |
| Compound | MW (g mol⁻¹) | Thiol pKₐ | HPLC purity | Onset of decomp. |
| 3‑Oxo‑5‑sulfanyl‑2,3‑dihydroisothiazole‑4‑carboxylic acid | 177.19 | 6.8 ± 0.2 | ≥98.0% | 178�°C |
| 3‑Oxo‑2,3‑dihydroisothiazole‑4‑carboxylic acid | 129.14 | – | ≥98.0% | 210�°C |
| 5‑Mercapto‑1,3‑thiazole‑4‑carboxylic acid | 161.20 | 5.3 ± 0.2 | ≥97.0% | 152�°C |
| 2‑Mercaptothiazole‑4‑carboxylic acid | 161.20 | 4.9 ± 0.2 | ≥97.5% | 155�°C |