|
HS Code |
637859 |
| Chemical Formula | C7H4N2O |
| Molar Mass | 132.12 g/mol |
| Appearance | Solid |
| Color | Typically white to off - white |
| Odor | May have a faint, characteristic odor |
| Melting Point | 275 - 277 °C |
| Solubility In Water | Slightly soluble |
| Solubility In Organic Solvents | Soluble in some organic solvents like DMSO, DMF |
| Stability | Stable under normal conditions |
| Hazard Class | Potential irritant, proper handling required |
As an accredited 1,2-Benzisot Hiazole-3-Ketone factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 1,2 - Benzisothiazole - 3 - Ketone packaged in 1 - kg containers for chemical use. |
| Shipping | 1,2 - Benzisothiazole - 3 - Ketone is typically shipped in well - sealed, corrosion - resistant containers. Packaging ensures protection from moisture and physical damage during transit, following strict chemical shipping regulations. |
| Storage | 1,2 - Benzisothiazole - 3 - Ketone should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, ignition sources, and direct sunlight. Store in a tightly sealed container to prevent moisture and air exposure, which could potentially lead to degradation. Avoid storing near reactive substances to prevent chemical reactions. |
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Production-scale preservation of water-based architectural coatings formulated with styrene-acrylic, pure acrylic, and vinyl acetate-ethylene binders demands a biocide that retains functional integrity across the alkaline pH spectrum where cellulosic thickener degradation by Pseudomonas spp. accelerates. The sodium or potassium salt of 1,2-Benzisothiazol-3-one (CAS 2634-33-5) provides this continuity, resisting hydrolytic ring-opening at pH values up to 12.0–12.5 in silicate-based mineral finishes and lime washes, environments in which chlorinated methylisothiazolinone derivatives undergo rapid nucleophilic deactivation. Dosage is executed during the letdown and tinting phase, post-grind, at a rate of 0.08% to 0.15% by total formulation weight, introduced under low-shear sweep agitation with a tip speed remaining below 5 m/s to minimize air entrainment and foam stabilization. The batch temperature must have decayed to below 45 °C from the dispersion plateau, as prolonged exposure to localized thermal gradients above 60 °C adjacent to the disperser blade can prematurely volatilize the co-solvent carrier, momentarily spiking the active concentration near the shaft and causing micro-gelation in acrylic colloids. Verification of in-can efficacy proceeds under accelerated storage protocols per ISO 11930 challenge test methodology adapted for non-cosmetic viscous suspensions, with acceptance criteria requiring a 3-log reduction in Enterobacter cloacae and Aspergillus brasiliensis inoculum within 72 hours. Compatibility with formaldehyde-scavenging reducing agents, particularly sodium sulfite added at 0.1–0.3% for indoor air quality compliance, must be confirmed via redox titration, as the electrophilic sulfur atom in the isothiazolone ring undergoes irreversible S-N bond scission when the oxidation-reduction potential of the matrix drops below -50 mV. Finished architectural products include interior latex paints certified under GB/T 9756-2018 and exterior clear wood varnishes meeting DIN EN 927-2 weathering resistance classifications. Why does BIT maintain long-term stability in high-pH cleaning formulations while other isothiazolinone derivatives undergo structural hydrolysis?The kinetic resilience of 1,2-Benzisothiazol-3-one in strongly alkaline cleaning concentrates—heavy-duty degreasers, high-caustic oven cleaners, and industrial floor strippers operating above pH 11—stems from the absence of a chlorine leaving group at the C-5 position of the heterocyclic ring. In mixtures where sodium or potassium hydroxide concentration exceeds 5% w/w, the half-life of a 3:1 CMIT/MIT blend collapses to less than 48 hours at 25 °C, whereas BIT retains more than 90% of its initial active content after 90 days as measured by HPLC-UV at 254 nm. The dominant degradation vector for BIT in this environment is not pH-driven hydrolysis but oxidative dimerization catalyzed by dissolved transition metal ions; consequently, the processing sequence must incorporate a chelation step using EDTA tetrasodium salt at 0.05% or equivalent aminocarboxylate prior to biocide injection to sequester trace copper and iron below 1 ppm. Addition is targeted in the post-neutralization cooling phase, after the incorporation of nonionic alcohol ethoxylate surfactants and amphoteric co-surfactants, at a loading of 0.05% to 0.10% on total batch mass, metered through a positive-displacement diaphragm pump into the recirculation loop of the blending vessel to ensure turbulent dispersion without localized concentration overshoot. Regulatory conformance falls under the EU Detergent Regulation (EC) No 648/2004, Annex VII, where the allergenic potential of the preserved formulation must be assessed via local lymph node assay data incorporated into the product safety dossier. End-use articles span industrial trigger-spray degreasers, liquid laundry detergent unit-dose packs, and automatic dishwashing gels stored in water-soluble polyvinyl alcohol film. Field Evidence of Hydrogen Sulfide Suppression and Biofilm Disruption in Full-Synthetic and Semi-Synthetic Metalworking Fluid ConcentratesRecirculating metalworking fluid systems present a chronic biological challenge in which sulfate-reducing bacteria and non-tuberculous mycobacteria establish resilient biofilms on sump walls, way covers, and internal coolant channels of CNC machining centers. In-use failure analysis of concentrates preserved solely with triazine-based formaldehyde releasers frequently identifies breakthrough odors from hydrogen sulfide generation when tramp oil layers create anaerobic microenvironments. Incorporating 1,2-Benzisothiazol-3-one into the concentrate at 0.15% to 0.30% by weight, introduced after the final co-emulsification of mineral oil, fatty acid soaps, and extreme pressure additives, delivers residual protection that transfers proportionally to the diluted working fluid at 5–10% concentration in water. The critical processing control point is the temperature during biocide introduction; dosing must be sequenced strictly after the exothermic neutralization of amine-based corrosion inhibitors has subsided and the bulk tank temperature has fallen below 45 °C to prevent wasteful losses of active compound through Michael-type addition reactions with excess mono- and triethanolamine, a side reaction that has been documented to consume between 5% and 12% of the added biocide when holding at 60 °C for 72 hours. Antimicrobial performance in the field is evaluated under ASTM E2275-19 for bacterial regrowth and fungal resistance using dip-slide monitoring with a threshold intervention limit of 10⁴ CFU/mL. German market compliance requires documentation aligning with TRGS 611 restrictions on secondary amine and formaldehyde emission limits during machining operations. Final product forms include extreme-pressure emulsifiable oils conforming to ASTM D7049 mist suppression categories and fully synthetic grinding fluids compatible with 7075 aluminum aerospace alloys. Pressure-sensitive adhesives manufactured from vinyl acetate-ethylene, carboxylated styrene-butadiene, and acrylic copolymer emulsions are uniquely susceptible to biodeterioration during in-process hold tanks prior to coating onto release liner, where the aqueous serum phase supports rapid proliferation of proteolytic and cellulolytic spoilage organisms that cleave the polymer backbone, causing an irreversible collapse in Brookfield viscosity from several thousand centipoise to below 500 cP. Post-polymerization addition of 1,2-Benzisothiazol-3-one at 0.10% to 0.15% on emulsion weight, executed after the residual monomer reduction stage catalyzed by tert-butyl hydroperoxide and sodium metabisulfite redox pairs has completed, provides a static antimicrobial barrier that does not interfere with the subsequent compounding of tackifier dispersions or fumed silica rheology modifiers. For adhesive constructions intended for indirect food-contact applications under FDA 21 CFR 175.105, the migration potential of the biocide from the dried adhesive layer must be calculated using a worst-case diffusion model assuming Fickian transport with a diffusion coefficient on the order of 10⁻¹² m²/s in the polymer matrix, confirming that the final non-detectable migration remains below the specific migration limit threshold. A documented formulation pitfall occurs when nano-scale zinc oxide or titanium dioxide pigments with Brunauer-Emmett-Teller surface areas exceeding 50 m²/g are incorporated without pre-passivation; the high-energy surface of these metal oxides adsorbs BIT from the aqueous phase within 24–48 hours, reducing the free biocide concentration in the supernatant by more than 60% and necessitating a compensatory concentration increase verified by liquid chromatography. Downstream finished goods include high-clarity film labels, bookbinding hot-melt edge adhesives, and UV-curable laminating films produced on wide-web coating lines with line speeds exceeding 300 m/min. Adsorption-Driven Depletion and Dosage Compensation Strategies for Aqueous Pigment and Mineral Filler SlurriesHigh-solids pigment slurries, particularly those based on ground calcium carbonate, calcined kaolin, and rutile titanium dioxide at solids contents above 65% w/w, function as potent adsorptive sinks for biocides due to the extensive solid-liquid interfacial area generated during wet comminution in horizontal media mills. The preservation strategy for these intermediates therefore cannot rely on nominal dosage guidelines derived from clear solutions; instead, the formulation must account for the adsorption isotherm of 1,2-Benzisothiazol-3-one onto the specific pigment surface. The table below summarizes the experimentally determined adsorption constants and compensating dosage adjustments required to maintain a minimum inhibitory free concentration above 50 ppm in the aqueous interstitial phase after 28 days of quiescent storage at 40 °C.
The process engineering solution to mitigate adsorption-induced depletion involves metering the BIT potassium salt solution directly into the recirculation loop of the horizontal bead mill via a progressive cavity pump, rather than surface-dosing into the letdown tank, thereby achieving maximum dispersion across the freshly generated particle surfaces before competing ions from dispersants such as sodium polyacrylate can occupy the active adsorption sites. The pH of the slurry must be buffered within ±0.5 units of the pigment's point of zero charge to minimize electrostatic attraction of the partially dissociated BIT molecule. Compliance for slurries destined for decorative paints references DIN EN ISO 787-9 for aqueous suspension pH determination and the EU Ecolabel criteria for indoor paints, which restrict the total volatile organic compound and semi-volatile organic compound loading attributable to the biocide package. Finished product types include pigment preparations for in-plant tinting systems, filler compounds for paper coating, and anti-corrosion primer bases. Mitigating the Combined Constraints of Phase Partitioning and Enzymatic Ring-Opening When Protease and Amylase Loadings Challenge BIT Integrity in Heavy-Duty Liquid DetergentsThe preservation of unit-dose liquid laundry detergents and high-surfactant multi-purpose cleaners containing encapsulated enzyme slurries—typically Bacillus-derived subtilisin protease and Thermomyces-sourced lipase and amylase blends—introduces two interrelated mechanisms of potential biocide failure that act synergistically in the packaged product. The first mechanism is thermodynamic: linear alkylbenzene sulfonate and alcohol ethoxysulfate micelles, which constitute 15–30% of the formulation, selectively partition hydrophobic isothiazolinones into the micellar pseudo-phase, effectively removing them from the aqueous continuous phase where planktonic microbial cells reside. BIT, with a measured octanol-water partition coefficient of approximately 1.1, retains a significantly higher interstitial water concentration compared to benzisothiazolinone derivatives with longer alkyl chains, maintaining a fractional aqueous availability exceeding 0.4 in a 20% surfactant matrix. The second mechanism is chemical: residual protease activity, even at the 0.1–0.5% level of non-encapsulated carryover from enzyme manufacturing, can catalyze the hydrolytic cleavage of the isothiazolone amide linkage under the warm, alkaline storage conditions common in tropical warehousing. To guard against this dual stress, the addition of 1,2-Benzisothiazol-3-one at 0.06% to 0.12% is scheduled as the penultimate step after the boric acid or sodium formate enzyme stabilization system has been homogenized and the final pH adjusted to 7.5–8.5 with citric acid, ensuring that the bulk temperature has relaxed below 35 °C to avoid hydrophobic denaturation of the enzyme tertiary structure upon contact with the biocide's glycolic co-solvent. Aquatic toxicity profiling as mandated by the EU Ecolabel for Laundry Detergents (Commission Decision (EU) 2017/1218) necessitates that the Chronic No-Observed-Effect Concentration for Daphnia magna supplied by the biocide manufacturer be incorporated into the Critical Dilution Volume calculation to remain below the permissible toxicity threshold. Finished goods encompass single-dose polyvinyl alcohol film pouches, high-efficiency front-loading laundry liquids, and fabric softening rinses. Synthetic latex manufacture—covering vinyl-acrylic, styrene-butadiene, and pure acrylic dispersions produced by seeded semi-continuous emulsion polymerization—generates a wet intermediate that must be held in surge vessels between the stripping column and spray-drying atomizer or drum-filling station, often at residual moisture contents above 45% and temperatures in the 30–40 °C range, ideal conditions for the proliferation of slime-forming Klebsiella and Pseudomonas species that foul downstream rotary atomizer wheels and plate heat exchangers. Injection of 1,2-Benzisothiazol-3-one into the latex transfer line at a dose of 0.05% to 0.15% by latex mass, accomplished through an in-line static mixer positioned after the final finishing chiller, arrests bacterial colony-forming unit counts below the 10³ CFU/mL threshold before the holding tank residence time exceeds 8 hours. A critical process compatibility test must be performed when the biocide is introduced into styrene-acrylic latices formulated with high levels of itaconic acid or other carboxyl-functional monomers, because the resulting increased anionic surface charge density on the latex particle can cause compression of the electrostatic double layer by the potassium counterion from the BIT salt, precipitating a detectable increase in the mean particle diameter as monitored by photon correlation spectroscopy under ISO 13320:2020. If the Z-average particle size shift exceeds +15 nm, a non-ionic ethoxylated stabilizer should be post-added to restore shear stability. VOC compliance for the final dry polymer powder destined for construction mortars must be cross-referenced against the residual biocide's boiling point contribution under GB 18582-2020 indoor decorating and refurbishing materials limits. Terminal product forms include redispersible polymer powders for tile adhesives, external thermal insulation composite system base coats, and self-leveling flooring compounds. |
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In-can and dry-film preservation strategies diverge sharply around pH stability and partition behavior. 1,2-Benzisothiazol-3-one (BIT, CAS 2634-33-5) occupies a narrow operational space where its thioether ring remains intact at pH values up to 12, whereas the widely used methylchloroisothiazolinone/methylisothiazolinone (CMIT/MIT) combination degrades via hydrolytic ring-opening above pH 8.5–9.0. This stability advantage makes BIT the dominant choice for high-alkalinity metalworking fluid central systems and styrene‑acrylic copolymer emulsions. However, BIT exhibits markedly slower kill kinetics against Pseudomonas aeruginosa compared to CMIT; minimum inhibitory concentrations (MICs) reported in technical literature typically range from 50–300 ppm active BIT versus 2.5–15 ppm active CMIT/MIT for planktonic bacteria. The trade-off is further modulated by water solubility. BIT dissolves to approximately 1.1 g/L at 20 °C, necessitating formulated liquid grades that incorporate dipropylene glycol to maintain homogeneous dosing. In contrast, the more polar CMIT/MIT salts remain freely miscible. Octylisothiazolinone (OIT), engineered for dry-film applications, is virtually water-insoluble (<0.05 g/L) and partitions strongly into binder phases; OIT is therefore unsuitable for bulk liquid preservation and is rarely applied below pH 7.5 due to accelerated alkaline hydrolysis.
| Property | BIT | CMIT/MIT (3:1 blend) | OIT |
|---|---|---|---|
| CAS | 2634-33-5 | 55965-84-9 | 26530-20-1 |
| Active content (typical liquid) | 85 % aqueous, 20 % glycol dispersion | 1.5–14 % in water | 45 % in glycol ether |
| Water solubility at 20 °C | ~1.1 g/L | Fully miscible | <0.05 g/L |
| pH stability window | 2–12 | 2–8.5 (rapid loss above 9) | 3–7.5 |
| Primary mode of action | Thiol-mediated enzyme inhibition; slow penetration | Multi-target electrophilic attack; fast kill | Lipophilic membrane disruption |
| Typical in-can use level (active) | 100–500 ppm | 2–15 ppm | Not used in-can |
| Common applications | Metalworking fluids, polymer emulsions, adhesives | Cosmetics, household cleaners, cooling towers | Film preservative for paints, plastics, wood |
These fundamental differences dictate that blending BIT with other actives is rarely straightforward. The nucleophilic thiolate group on BIT renders it susceptible to deactivation by dissolved hydrogen sulfide or mercaptans; formulations containing sulfurized extreme‑pressure additives in cutting oils can consume active BIT, requiring real-time titration monitoring via iodometric back‑titration per DIN 38409-7 to maintain target residual concentration.
When BIT Replaces CMIT/MIT in High-pH Styrene-Acrylic EmulsionsProduction-scale preservation of architectural coatings increasingly shifts toward zero‑VOC, aldehyde‑free biocide packs, pushing formulators to substitute CMIT/MIT with BIT in styrene‑acrylic binders neutralized with ammonia or sodium hydroxide. In a model styrene‑butyl acrylate emulsion at pH 9.8 and 50 °C storage, accelerated stability testing per ASTM D2574-16 shows that BIT at 200 ppm active maintains a sterility count of <10 CFU/mL after 28‑day repeated inoculation with a mixed bacterial consortium, while a CMIT/MIT control loses efficacy within 72 h due to 3‑chloro‑isothiazolone ring hydrolysis. The difference is not merely kinetic: mass‑balance HPLC analysis of the headspace above CMIT‑treated emulsion detects chlorinated methacrylic acid cleavage products, whereas BIT breakdown under identical conditions is undetectable. Still, formulators must account for the slow ingress of BIT through Gram‑negative outer membranes; in heavily contaminated plant tanks with biofilm, a single shock dose of 400 ppm active BIT is followed by a 48‑hour lag before log‑reduction exceeds 3. This demands a process hold step that a CMIT/MIT option might avoid entirely.
On twin‑screw extruded compounded masterbatches where residual preservative is added post‑polymerization via a liquid injection nozzle at the pelletizer throat, BIT’s limited aqueous solubility creates a processing constraint. Undissolved BIT particles migrating to the surface of styrene‑acrylic pellets have been observed on lines equipped with underwater pelletizers when the injection solution concentration exceeds 2.5 wt% BIT in the carrier dipropylene glycol. Maintaining a maximum concentration of 2.3 wt% and incorporating an in‑line static mixer with 16 helical elements eliminated visible particle specks, as verified by scanning electron microscopy. Published data for this specific downstream configuration remains limited, but operators report that pre‑dilution loops must be temperature‑controlled to 35–40 °C to avoid cold‑crystallization of the BIT‑glycol concentrate.
| Parameter | BIT 85 % Aqueous | BIT 20 % Glycol Dispersion | Test Method |
|---|---|---|---|
| Active content (wt%) | 84.0–86.5 | 19.5–20.5 | Iodometric titration / HPLC |
| Density at 20 °C (g/cm³) | 1.30–1.33 | 1.12–1.15 | Oscillating U‑tube |
| pH (neat) | 8.0–9.5 | 6.0–8.0 | pH meter with glass electrode |
| Appearance | Clear amber to brown liquid | Pale yellow to amber dispersion | Visual; no phase separation after 72 h at 5 °C |
| Freezing point / pour point | <−10 °C | −20 °C | DSC / ASTM D97 |
| Heavy metals (as Pb) | <10 ppm | <5 ppm | ICP‑OES |
Storage stability data under IBC conditions confirm that the 85 % aqueous solution retains >95 % of initial assay after 12 months at 25 °C when protected from strong reducing agents and continuous UV exposure. Lid‑open drum simulations at 40 °C and 75 % RH result in surface skinning within 72 h; nitrogen‑blanketed totes eliminate this failure mode.
In-can preservation of water‑based adhesives demands rapid kill kinetics against re‑contamination introduced by recycled packaging. Yet plant trials on a vinyl acetate‑ethylene (VAE) copolymer dispersion with pH 4.2 revealed that BIT at 150 ppm active was insufficient to suppress yeast growth after 14‑day cyclic inoculation, whereas a synergistic blend of BIT and a formaldehyde‑releaser provided <10 CFU/g protection for the same period. This outcome illustrates BIT’s well‑documented gap against fungi, particularly Candida spp., when used as a standalone. Consequently, many registered preservative packs listed under BPR (Biocidal Products Regulation) Article 95 combine BIT with benzimidazole carbamates or pyrithione derivatives. Compatibility verification becomes critical: the chelating character of pyrithione zinc can destabilize BIT’s thione‑thiol tautomerism, leading to precipitation of a zinc‑BIT complex if the zinc ion concentration exceeds 50 mg/L in the wet‑state formulation. Operator logs from a lamination adhesive compounding line noted filter blockage when the zinc‑containing co‑biocide was charged before BIT; reversing the addition sequence—BIT first, allowed to disperse fully for 20 min under 600 rpm dissolver speed—resolved the incompatibility.Metalworking fluid sumps exceeding 20 000 L with recirculation rates of 100–150 L/min present a severe test for BIT persistence due to the compound’s affinity for tramp oil and its slow aqueous diffusion coefficient. In a field assessment conducted on a central grinding fluid system using a soluble oil at 6 % v/v, the half‑life of BIT was reduced to 12–14 days compared to a laboratory‑predicted 35 days, attributed to microbial consumption and nucleophilic scavenging by sulfurized fatty esters. The facility implemented an automated dosing protocol using an inline ORP probe calibrated to maintain −250 mV to −300 mV, realizing a steady‑state BIT concentration of 185–210 ppm as quantified by UV‑detection at 326 nm following solid‑phase extraction. Under this feedback control, ATP bioluminescence readings remained <150 RLU/mL over a 6‑month monitoring period, a threshold associated with absence of slime formation in this particular system configuration.