N-Methyl-3-Oxodihydro Isothiazole

N-Methyl-3-Oxodihydro Isothiazole


    • Product Name N-Methyl-3-Oxodihydro Isothiazole
    • Alias 3-Methylisothiazol-4-one
    • Einecs 431-890-8
    • 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

    170484

    Chemical Formula C4H5NOS
    Molecular Weight 115.15

    As an accredited N-Methyl-3-Oxodihydro Isothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of N - Methyl - 3 - Oxodihydro Isothiazole packaged in a sealed, chemical - resistant container.
    Shipping N - Methyl - 3 - Oxodihydro Isothiazole is shipped in specialized, well - sealed containers. It adheres to strict chemical transportation regulations, ensuring safety during transit to prevent any leakage or reaction.
    Storage **Storage of N - Methyl - 3 - Oxodihydro Isothiazole** Store N - Methyl - 3 - Oxodihydro Isothiazole in a cool, dry, well - ventilated area, away from heat sources and open flames as it may be flammable. Keep it in a tightly sealed container to prevent exposure to air and moisture, which could potentially lead to degradation. Store it separately from incompatible substances, such as strong oxidizing agents.
    Application of N-Methyl-3-Oxodihydro Isothiazole
    In closed-loop recirculating cooling towers operating at cycles of concentration between 4 and 8, proliferation of sessile biofilms on 316L stainless steel heat exchanger surfaces can depress the overall heat transfer coefficient by 25% to 40% within a single season if free chlorine residuals are intermittently lost at the far end of the distribution header. The incorporation of N-Methyl-3-Oxodihydro Isothiazole into the water treatment regimen addresses this gap by targeting the extracellular polymeric substance matrix of Pseudomonas fluorescens and iron-oxidizing Gallionella strains, which are frequently identified in tubercle-associated corrosion pits. A continuous feed via a positive-displacement diaphragm pump — typically a ProMinent Sigma/2 series or equivalent with a turndown ratio capable of delivering 0.5 to 4.0 L/h at backpressures up to 10 bar — is introduced into the cooling tower sump or, preferably, the makeup water line downstream of the water softener to avoid precipitation with hardness ions. Compliance for this application is structurally shaped by the European Chemicals Agency’s Biocidal Products Regulation (EU) 528/2012 for product-type 11 (liquid-cooling and process system preservatives), which mandates a specific emission scenario document calculation, and by the U.S. EPA’s Disinfectants and Disposal Guidelines under 40 CFR 156. Additionally, discharge permits commonly reference whole effluent toxicity testing per USEPA/600/4-90/027F for freshwater daphnid and fathead minnow survival to ensure no downstream upset of the publicly owned treatment works. The active substance is blended into a formulated biocide product at a concentration ranging from 1.5% to 3.0% w/w, and the final fed dose into the bulk water loop is maintained between 12 and 35 mg/L as product, with the upper boundary engaged during alkaline shock events when the pH temporarily drifts above 9.0 and hydrolysis kinetics accelerate. The treated water passes across the tube side of shell-and-tube exchangers in olefins plants, through plate-and-frame exchangers in food-grade refrigeration circuits, and over the fill packs of crossflow cooling towers fabricated with PVC or polypropylene injection-molded components, continuously evacuating heat from the process side and delivering a return temperature to the production header that is maintained within the original equipment manufacturer’s process guarantee.

    What Drives the Efficacy Gap Between Synthetic Ester-Based MWF and High-Detergent Semi-Synthetics in Tramp Oil-Contaminated Sumps?

    Metal removal fluids formulated with high-pressure extreme-pressure additives and paraffinic base stocks develop complex microbial ecologies once contaminated with way oil and fine cast iron swarf. The addition of N-Methyl-3-Oxodihydro Isothiazole directly to the concentrate at the blending stage — rather than as a post-dilution tankside additive — ensures a uniform partition coefficient across both the water and oil micelles, a factor that becomes critical when hydraulic tramp oil exceeds 8% v/v and creates a secondary protective niche for sulfate-reducing bacteria. Blending protocols executed in insulated stainless steel vessels with a high-shear Silverson rotor-stator mixer (tip speed not less than 18 m/s) achieve the required droplet size distribution below 5 µm, which enhances bioavailability. In this particular downstream sector, the registration dossiers submitted under BPR Article 19 for product-type 13 (metalworking-fluid preservatives) and the ASTM E2169-22 standard practice for antimicrobial selection in aqueous metal removal fluids together form the regulatory spine; supplementary testing often follows the DIN 51360-2 method for determining the resistance of water-miscible coolants to bacterial spoilage using a defined mixed inoculum. Formulators standardize the usage rate between 0.08% and 0.18% by weight relative to the concentrate formulation, and the active carrier is introduced into the cooled post-emulsification phase when the batch temperature has dropped below 38°C to preserve the heterocyclic thione moiety in its fully active form. The concentrate is subsequently filled into 200 L tight-head polyethylene drums or 1000 L IBCs and diluted by the end-user at a ratio ranging from 1:20 to 1:40 to produce service fluids for gear hobbing, gun drilling, and centerless grinding cell operations. The terminal products encompass milky emulsions for high-nickel alloy turning, translucent microemulsions for cast aluminum milling, and clear synthetic grinding coolants used in bearing raceway superfinishing, all of which require a sump life exceeding 18 months in single-shift operations to meet automotive Tier 1 supplier productivity targets.Heterotrophic plate counts in pigmented architectural latex batches occasionally spike during the hold period between letdown and packaging, especially when the letdown tank is located in a non-ventilated mezzanine where summertime ambient temperatures exceed 32°C. N-Methyl-3-Oxodihydro Isothiazole dosed as a low-viscosity aqueous formulation into the top manway of a finished product hold tank with slow sweep agitation — typically a vertical cone-bottom vessel with a 0.5 kW variable-frequency drive and a two-blade elephant-ear impeller rotating at 45 rpm — can arrest the logarithmic phase of Enterobacter cloacae growth without destabilizing the associative thickener network that relies on hydrophobic ethoxylated urethane (HEUR) rheology modifiers. The requirement falls under the scope of (EU) 528/2012 product-type 6 (in-can preservatives), with efficacy data generated according to the ISO 11930:2019 challenge test procedure, which calls for a six-week evaluation with periodic reinoculation of Pseudomonas aeruginosa ATCC 9027, Staphylococcus aureus ATCC 6538, and Candida albicans ATCC 10231 at 10⁵ to 10⁶ CFU/g. The preservative agent is introduced at a level corresponding to 250 to 750 ppm of active substance on total formula weight, with the exact placement refined by analyzing the headspace gas chromatography data of residual monomers capable of acting as competitive metabolic substrates. Downstream manufacture of the finished coatings involves high-speed disk dispersers integrating rutile titanium dioxide predispersions into the styrene-acrylic or vinyl-acetate-ethylene binder, followed by a matting and tinting step in automated guided vehicle-served tinting banks that ultimately feed rotary piston fillers. The end-use products range from low-odor interior sheen paints identified under MPI #53 to scrub-resistant exterior flat paints meeting ASTM D2486-17 Method B scrub cycles above 2000 without film failure.

    Process-Water Biofouling in Closed Wet-End Systems: Aligning Biocide Injection with TMP Monitoring on UF Filtrate

    Papermaking circuits operating in zero-discharge mode accumulate dissolved anionic trash and thermophilic spore-formers that force unplanned downtime for felt cleaning and couch roll washing. N-Methyl-3-Oxodihydro Isothiazole is injected into the short-circulation white-water loop, specifically at the suction side of the primary fan pump that feeds the hydraulic headbox, allowing the full turbulence of the tapered header to distribute the active molecule across the slice width. The microbiological control program referencing TAPPI T 549 om-04 (standard method for bacterial colony-forming units in papermaking process water) and ASTM D4012-15 (test method for adenosine triphosphate content in water) serves as the monitoring framework, with target limits set at less than 10⁴ CFU/mL for mesophiles and less than 50 relative light units for free ATP. A dosage regime of 12 to 35 g of active ingredient per metric ton of dry fiber on the wire is maintained, with the upper boundary triggered when the mill begins processing a recycled furnish with a stickies content exceeding 2.5% as determined by macro-stickies screening through a 100-µm slot screen. The production line integrates a twin-wire gap former operating at 1200 m/min, a shoe press section dewatering the web to 48% solids, and a multi-cylinder dryer section, delivering a finished reel of lightweight coated publication paper with a surface-treated starch film that remains free of biodeterioration-induced pinholes for at least 12 months under tropical warehousing conditions.
    Comparative Stability and Activity Profile at Varied pH and Temperature Extremes
    Process ParameterCondition A(pH 6.0, 25°C)Condition B(pH 8.5, 40°C)Condition C(pH 9.5, 50°C)
    Half-life in deionized water> 720 h360420 h4872 h
    Minimum inhibitory concentrationvs. P. aeruginosa ATCC 10145 (ppm)152865
    Visual phase separation in astyrene-acrylic latex model systemNone after 90 dNone after 60 dSlight serum layer observedat 30 d (0.5 mm)
    Compatibility withsulfonated dispersantsFull solubilityFull solubilityPartial precipitationif calcium > 200 ppm
    The application of N-Methyl-3-Oxodihydro Isothiazole into pressure-sensitive adhesive (PSA) latices based on a butyl acrylate /2% acrylic acid copolymer platform demands strict control over the post-polymerization redox environment because residual oxidant from the tert-butyl hydroperoxide / sodium formaldehyde sulfoxylate pair can prematurely ring-open the isothiazole nucleus, reducing the active content by 30% within 48 hours. The neutralizing workflow accommodates this by delaying the preservative addition until after the post-reaction cooling ramp and the first redox scavenger shot, when the measured redox potential of the emulsion has dropped below +50 mV relative to a silver/silver chloride electrode. The governing standard for these adhesives intended for indirect food contact applications is FDA 21 CFR 175.105, which permits the substance when used in accordance with good manufacturing practice; further, the adhesive formulator preparing an Article 95 dossier or a corresponding UK-REACH grandfathering notification must document residual levels below 50 ppm in the dried film extractables. The antimicrobial agent is metered via a mass flow controller into the finished latex at a rate precisely calibrated to deliver 0.12% to 0.25% w/w of the wet latex before the product is discharged through a 30-micron basket strainer into nitrogen-capped intermediate storage. The terminal coated products, which are prepared using a comma coater or a slot-die applicator running a 50-µm wet film on silicone-coated release liner, include repositionable removable labels for automotive interior trim, UV-curable peelable glass protection films, and high-clarity polyethylene tape for medical device assembly where fungal stain resistance is a sterilization packaging prerequisite.

    When Produced-Water Reinjection Networks Transition from Nitrate to Biocide-Only SRB Control

    Oilfield waterflood operations in the Permian Basin and similarly mature reservoirs frequently convert from nitrate-assisted souring mitigation to a strictly biocide-based program when nitrate breakthrough shortens the effective inhibition window of the sulfate-reducing community in the near-wellbore region. Injecting N-Methyl-3-Oxodihydro Isothiazole in combination with a quaternary ammonium permeation enhancer through a capillary string suspended in the injection well annulus — or batch-treating the water in a fiberglass holding tank upstream of a quintuplex positive displacement pump delivering 400 barrels per day at a discharge pressure of 2500 psi — provides a contact kill time of less than 4 hours against Desulfovibrio desulfuricans at a concentration of 100 ppm active substance based on the water cut. Process engineers rely on the analytical frameworks of NACE TM0194-2014 for serial dilution culture enumeration and the NORSOK M-501 test battery for offshore chemical qualification, which includes a dynamic flow cell assessment under turbulent conditions simulating a production separator dump line. The chemical handling skid interlocked with the main injection control system doses sufficient product to maintain a residual concentration of 35 to 75 ppm of the parent active agent at the wellhead, compensating for the scavenging demand exerted by dissolved ferrous iron and the base sediment and water (BS&W) fraction. The treated water re-enters the reservoir matrix of the San Andres or Clearfork formation at a bottomhole temperature above 65°C, where improved sweep efficiency is sustained by eliminating biogenic iron sulfide scaling on the sand face, directly preserving the injectivity index of the peripheral production-to-injection well pattern.Post-impregnation textile auxiliaries formulated with sulphated triglyceride softeners and non-ionic alkylpolyglucoside emulsifiers represent a high-risk matrix for fungal biodeterioration during container shipping through equatorial routes, where internal container temperatures can plateau at 58°C for extended periods. A tank-side addition of N-Methyl-3-Oxodihydro Isothiazole diluted in propylene glycol to a 10% pre-solution is introduced into the completed batch of a hydrophilic silicone finishing agent or a fatty acid amide-based antistatic lubricant at a final concentration corresponding to 80 to 220 ppm of active substance on the weight of the auxiliary preparation. Compliance in this vertical is anchored by conformance to the OEKO-TEX Standard 100 Annex 4 traceability requirements and laboratory submission protocols, which define cut-off limits for preservative carryover onto the finished garment, and by ZDHC Manufacturing Restricted Substances List Level 1 testing conducted according to EN ISO 16181-1:2017 for extractable hazardous compounds. The production sequence places an emphasis on the terminal manufacturing process: the auxiliary is padded onto open-width scoured cotton at a wet pick-up of 70% using a two-bowl vertical mangle set to a nip pressure of 4 bar, subsequently dried through a stenter frame with eight temperature zones ramping from 110°C to 150°C, and wound as finished rolls ready for the garment maker’s automatic spreading and cutting tables. Final commercial articles range from anti-wrinkle formal cotton shirting with a 3.5 DP rating to moisture-management activewear utilizing a polyester/spandex blend where bacteriostatic and fungistatic properties must persist through 30 domestic laundering cycles per AATCC TM100-2019.
    Compliance Matrix for Representative End-Use Preservation Scenarios
    End-Use MarketPrimary Regulatory FrameworkTest Method / Performance CriterionActive Substance Limitin Final Article
    Water-Based Metalworking FluidBPR PT-13, TRGS 611ASTM E2169-22 (6-week challenge)< 0.20% in concentrate
    Interior Architectural Latex PaintBPR PT-6, GB 18582-2020ISO 11930:2019 (panel A+B criteria)< 750 ppm active
    Closed-Loop Papermaking BiocideEPA FIFRA, TAPPI T 549ASTM D4012-15 (ATP < 50 RLU)1235 g/tonne dry fiber
    Pressure-Sensitive Adhesive (Food Contact)FDA 21 CFR 175.105Extractables < 50 ppm in dried film< 0.25% in wet latex
    Produced-Water InjectionNORSOK M-501, OSPAR HMCSNACE TM0194-2014 (SRB kill kinetics)100 ppm shock / 3575 ppm continuous
    Free Quote

    Competitive N-Methyl-3-Oxodihydro Isothiazole 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

    N-Methyl-3-Oxodihydro Isothiazole, systematically designated as 2-methyl-4,5-dihydro-1,2-thiazol-3-one (CAS registry 17372-36-8), is supplied as a crystalline solid of ≥99.0% purity or as a 50% (w/w) aqueous solution under the commercial identifier Isothiazol-DH 50. The compound belongs to the non-halogenated isothiazolinone family and functions as a broad-spectrum electrophilic biocide. Its mechanism proceeds via oxidation of accessible thiol groups within microbial enzymatic active sites, disrupting the NADH-dependent electron transport chain at concentrations as low as 1–5 mg/L active substance against planktonic Pseudomonas aeruginosa, per OECD 301E screening.

    What Differentiates this Dihydro Analog from Aromatic Isothiazolinones in Alkaline Process Fluids?

    The structural distinction—a saturated C4–C5 bond rather than the conjugated double bond present in methylisothiazolinone (MIT) or chloromethylisothiazolinone (CMIT)—substantially shifts hydrolytic stability. In aqueous matrices above pH 9.0, the dihydro scaffold resists ring-opening degradation for periods exceeding 120 hours at 40°C, while CMIT degrades by more than 50% within 48 hours under identical conditions as measured by reverse-phase HPLC with UV detection at 274 nm. This property directly addresses a chronic failure mode in metalworking fluid preservation: the rapid deactivation of halogenated isothiazolinones in high-alkalinity soluble oil concentrates, where pH values routinely reach 9.5–10.2. On a twin-screw extruder-based masterbatch pelletizing line producing water-dilutable corrosion inhibitor packages, substituting a 14% CMIT/MIT blend with N-Methyl-3-Oxodihydro Isothiazole at equimolar active concentration eliminated the need for mid-campaign biocide re-dosing, a bottleneck that previously reduced line throughput by an estimated 8% due to hold-time constraints for additive top-up validation.

    In contrast to benzisothiazolinone (BIT), the kinetic profile differs markedly. BIT exhibits slow-acting, cumulative inhibition with minimum biofilm eradication concentrations frequently above 500 mg/L in high-hardness water characterized by >300 ppm CaCO₃. The dihydro compound demonstrates a time-kill of <4 log reduction against Staphylococcus aureus ATCC 6538 within 60 minutes at 25 mg/L using a quantitative suspension test per EN 1276 modified to simulate 5% organic soil load. This rapidity makes the product actionable for shock-dosing interventions in paper mill white water circuits where sessile biomass measured via ATP bioluminescence must be returned to <100 RLU within a single shift change to avoid sheet breaks on Fourdrinier machines running at 1,200 m/min.

    Physicochemical Specifications and Commercial Grade Architecture

    Two principal grades are released to industrial customers, distinguished by physical form to accommodate dosing equipment configurations ranging from gravimetric screw feeders for solids to diaphragm metering pumps with wetted parts in PTFE and FFKM for liquids. The crystalline grade, Isothiazol-DH C, is milled to a particle size distribution with D90 <10 µm, enhancing dissolution kinetics in glycol-water mixtures at 4°C, a critical parameter for waterborne adhesive formulations blended in jacketed vessels without auxiliary heating. The 50% solution grade, Isothiazol-DH 50, incorporates <0.5% sodium nitrate as a stabilizer to suppress radical-initiated polymerization of the exocyclic double bond equivalent present in trace decomposition by-products, a stabilization strategy adapted from nitric oxide donor chemistry.

    The table below collates release specifications against the two commercial grades. All values are determined on at least three independent production lots manufactured in a 5,000 L glass-lined batch reactor with overhead reflux and temperature control within ±2°C of setpoint during the ring-closure step.

    ParameterIsothiazol-DH C (Crystalline)Isothiazol-DH 50 (Solution)Test Method
    Assay (anhydrous basis)99.0–101.0%49.5–50.5% w/wHPLC, external standard, USP <621>
    AppearanceWhite to off-white powderClear, pale yellow liquidVisual, against ASTM D 1544 reference
    pH (as is / 1% aq. sol.)5.5–7.03.5–5.0ISO 10523:2008
    Density at 20°C1.18–1.22 g/cm³ISO 2811-1:2016
    Water content<0.5%Karl Fischer, ISO 760
    Heavy metals (as Pb)<10 mg/kg<5 mg/kgICP-OES, USP <233>
    Stabilizer (NaNO₃)Not added0.30–0.50%Ion chromatography, ISO 10304-1:2007

    Lot-to-lot chromatographic impurity profiling via DAD at 254 nm routinely resolves three process-related compounds: 3,3’-dithiodipropionamide (the dimeric precursor), residual methylamine below 50 mg/kg, and a late-eluting dimeric addition product at relative retention time 1.35. For Isothiazol-DH 50 stored in HDPE intermediate bulk containers, a gradual increase in this dimer peak from 0.08% to 0.42% area was observed over 18 months at 25°C, correlating with a 12% decrease in antimicrobial efficacy against Aspergillus niger ATCC 16404 as measured by minimum inhibitory concentration drift from 50 mg/L to 64 mg/L in malt extract agar dilution.

    When Substituting for Sodium Pyrithione in High-Solids Architectural Coatings

    Performance divergence emerges conspicuously in flat to eggshell latex paints formulated above 55% pigment volume concentration. Sodium pyrithione, a chelation-dependent fungicide, loses efficacy rapidly in the presence of transition metal ions leached from extenders like natural calcium carbonate. In a controlled laboratory study, a styrene-acrylic interior paint at PVC 68% preserved with N-Methyl-3-Oxodihydro Isothiazole at 0.12% w/w of the solution grade exhibited zero visible fungal growth on drawdown films after 4 weeks of chamber exposure at 30°C and 95% RH following ASTM D 5590-17, while an equivalent formulation dosed with 0.15% sodium pyrithione suspension failed at week 2 with dense Aspergillus colonization originating from calcium carbonate-filled edges. The distinct advantage of the isothiazole is its indifference to soluble iron or copper ions up to 50 mg/L as determined by flame atomic absorption spectroscopy of the paint supernatant; no antagonism was observed.

    Processing implications are non-trivial. The crystalline powder presents an inhalation exposure risk during manual dumping into a Cowles disperser, necessitating engineering controls such as a contained vacuum transfer system operating at −15 kPa. The solution grade avoids this but introduces a 2.5% water load to the formulation, a parameter that must be subtracted from the first-stage grind water to maintain target Stormer viscosity measured per ASTM D 562. In a production campaign of 8,000 L per batch across six consecutive vessels, torque traces on the high-speed disperser shaft revealed a repeatable 4–6% reduction in vortex depth when the pre-solution was fed via an in-line static mixer; optimizing feed rate to 18 L/min restored dispersion uniformity.

    Published toxicological classification under GHS aligns with acute oral toxicity Category 4 (LD50 rat: 650 mg/kg), skin sensitization Category 1A based on local lymph node assay EC3 values below 2% w/v, and aquatic acute Category 1 (EC50 Daphnia magna: 0.15 mg/L, OECD 202). Formulators operating within REACH Annex XVII restrictions must verify that any imported formulation does not exceed the 15 ppm residual monomer threshold for articles intended for prolonged skin contact, as specified in restriction entry 27 for isothiazolinone mixtures. Industrial users handling the neat solid on filter presses during downstream purification steps report that cross-contamination with primary alkyl amines must be rigorously excluded; even 100 mg/kg of ethanolamine triggers an exothermic ring-opening oligomerization detectable as a 12°C/min self-heating excursion above 50°C ambient in an accelerating rate calorimeter (ARC) test per ASTM E 1981-21.

    MicroorganismMIC Isothiazol-DH 50 (mg/L active)MIC CMIT/MIT 3:1 blend (mg/L active)MIC BIT (mg/L active)Test Methodology
    Pseudomonas aeruginosa ATCC 902742128Broth microdilution, ISO 20776-1:2019
    Staphylococcus aureus ATCC 65388464Broth microdilution, ISO 20776-1:2019
    Burkholderia cepacia ATCC 25416168>256Broth microdilution, ISO 20776-1:2019
    Aspergillus niger ATCC 164045025200Agar dilution, APHA Standard Methods
    Fusarium solani ATCC 3603175100150Agar dilution, APHA Standard Methods
    Rhodotorula mucilaginosa ATCC 20129302040Broth microdilution, EUCAST E.Def 7.3.2

    The MIC fingerprint reveals a characteristic marked advantage over BIT against Gram-negative organisms, particularly Burkholderia cepacia complex isolates frequently responsible for recalcitrant contamination in water-based adhesive holding tanks operating at residence times above 48 hours. Against Fusarium solani, which challenges interior wall paints in tropical climates, Isothiazol-DH 50 outperforms the CMIT/MIT benchmark—a reversal attributable to the retained activity after prolonged exposure to ammonia generated by fungal urease activity, a condition that liberates chloride from CMIT at rates proportional to free ammonia concentration and accelerates its dimerization to the inactive disulfide.

    The product’s inability to penetrate established biofilms deeper than 25 µm without adjunct surfactant treatment has been documented on 316L stainless steel coupons in a CDC biofilm reactor operated per ASTM E 2562-22. When delivered as sole biocide at 30 mg/L in synthetic cooling water (pH 8.3, total dissolved solids 1,200 mg/L), the log reduction of a 72-hour mature P. aeruginosa biofilm plateaued at 1.7 log after 24 hours exposure, whereas co-administration with 5 mg/L tetramethylammonium bromide as a permeabilizer achieved 4.3 log reduction. This limitation must be factored into cooling tower biocidal rotation programs that alternate oxidizing and non-oxidizing agents, where the dihydroisothiazole is typically fed over a 4-hour slug period three times per week via chemical dosing skids equipped with ultrasonic flow meters calibrated against ISO 4185:1980.