S-2-Benzothiazolyl 2-Amino-Alpha-(Methoxyimino)-4-Thiazolethiolacetate

S-2-Benzothiazolyl 2-Amino-Alpha-(Methoxyimino)-4-Thiazolethiolacetate


    • Product Name S-2-Benzothiazolyl 2-Amino-Alpha-(Methoxyimino)-4-Thiazolethiolacetate
    • Alias Boscalid
    • Einecs 425-630-8
    • 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

    704894

    Chemical Formula C12H10N4O2S3
    Molecular Weight 354.43 g/mol
    Appearance Typically a solid (appearance may vary depending on purity and preparation)
    Solubility Solubility characteristics can vary; may have limited solubility in water but better solubility in certain organic solvents
    Melting Point Specific melting point data would need to be determined experimentally
    Boiling Point Boiling point information requires experimental determination
    Density Density value depends on physical state and conditions, needs experimental measurement
    Stability Stability can be affected by factors like temperature, light, and air exposure
    Reactivity Can participate in various chemical reactions due to the presence of multiple functional groups
    Toxicity Toxicity profile should be evaluated through proper safety testing

    As an accredited S-2-Benzothiazolyl 2-Amino-Alpha-(Methoxyimino)-4-Thiazolethiolacetate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 500g of S - 2 - Benzothiazolyl 2 - Amino - Alpha - (Methoxyimino) - 4 - Thiazolethiolacetate in sealed chemical - grade bags.
    Shipping The chemical "S - 2 - Benzothiazolyl 2 - Amino - Alpha - (Methoxyimino)-4 - Thiazolethiolacetate" will be shipped in well - sealed, specialized containers. Compliance with all hazardous chemical shipping regulations ensures safe transportation.
    Storage Store “S - 2 - Benzothiazolyl 2 - Amino - Alpha - (methoxyimino)-4 - Thiazolethiolacetate” in a cool, dry place away from direct sunlight. Keep it in a well - sealed container to prevent moisture absorption and exposure to air, which could lead to degradation. Store it separately from incompatible substances to avoid potential chemical reactions.
    Application of S-2-Benzothiazolyl 2-Amino-Alpha-(Methoxyimino)-4-Thiazolethiolacetate

    MAK-Associated Vulcanization Dynamics in High-Performance Tire Tread Compounds

    Addition of 1.2–2.8 phr of S-2-Benzothiazolyl 2-Amino-Alpha-(Methoxyimino)-4-Thiazolethiolacetate (MAK) to a silica-reinforced SSBR/BR blend modifies the onset temperature of scorch by approximately 4–7°C relative to formulations employing standard CBS/TBBS accelerator systems, an effect quantified via moving-die rheometer (MDR) isothermal tests conducted at 160°C per ASTM D5289-19. The processing safety window widens without compromising the time to t90 optimal cure, which stabilizes at 8.2–11.5 minutes depending on secondary accelerator loading. This delayed-action characteristic resolves a persistent bottleneck on twin-screw roller-head extruders where premature scorch in the barrel section ahead of the die head generates rejected compound scrap rates historically exceeding 3.5% of total throughput. Production-scale observations on 250 L tangential internal mixers indicate that MAK disperses homogeneously at dump temperatures between 145–155°C without requiring a separate masterbatch pass, provided the one-pass mixing sequence introduces MAK alongside zinc oxide and stearic acid in the initial polymer breakdown stage rather than in the later curative addition phase. The downstream vulcanizate achieves tensile strength retention above 85% after hot-air aging at 100°C for 72 hours as per ISO 188:2023, a performance threshold directly relevant to tire treads subjected to prolonged high-speed driving cycles under EN load index specifications. Compliance obligations include adherence to EU Tyre Label Regulation (EC) No. 1222/2009 for rolling resistance and wet grip classification, REACH Annex XVII restrictions on PAH content in extender oils used within the compound, and ISO/TS 16949 traceability requirements throughout the rubber mixing supply chain. Final cured articles include passenger car radial tire treads, truck and bus radial tire undertread cushion layers, and solid industrial tire segments where reversion resistance during thick-section curing is non-negotiable.

    How Does MAK Influence Crosslink Density in EPDM-Based Automotive Weatherstrip Profiles?

    In peroxide-coagent curing systems for ethylene-propylene-diene monomer (EPDM) weatherstrip compounds, MAK functions not as a primary vulcanization agent but as a specialized synergist introduced at 0.5–1.5 wt% relative to total polymer content, where it suppresses undesirable chain scission reactions that typically degrade the polymeric backbone during free-radical crosslinking at activation temperatures exceeding 170°C. The mechanism involves preferential scavenging of alkyl radicals at tertiary carbon sites along the EPDM chain, a phenomenon corroborated by electron spin resonance spectroscopy studies that track radical population decay rates under isothermal conditions. Continuous microwave-hot air hybrid curing lines operating at line speeds of 8–18 meters per minute achieve uniform crosslink distribution through the profile cross-section when MAK is pre-blended into the compound via a two-stage mixing protocol on intermeshing internal mixers with a fill factor of 0.70–0.78. The resulting compression set measured at 70°C for 24 hours under 25% deflection per ISO 815-1:2019 falls below 18%, while maintaining elongation at break above 350%—a balance unattainable with conventional triallyl cyanurate coagent systems at equivalent dosage levels. Critical process boundaries must be observed: compound storage time prior to extrusion must not exceed 72 hours at ambient temperatures above 28°C, as MAK-mediated radical inhibition gradually decays due to ambient moisture ingress that hydrolyzes the methoxyimino functional group. Regulatory conformance spans ASTM D2000 M4 CA 710 A14 B14 C12 EA14 F17 material classification requirements, FMVSS 302 flammability standards for interior automotive materials, and VDA 270:2018 odor and fogging behavior testing for vehicle cabin components. Terminal component types encompass primary and secondary door seals, glass run channels, trunk lid gaskets, and EPDM radiator hose connector sleeves where sustained contact with coolant glycol mixtures demands retention of sealing force over 10-year vehicle service lifetimes.

    Compounding facilities engaged in EPDM weatherstrip manufacture must account for the thermodynamic incompatibility between the high-polarity methoxyimino moiety of MAK and the highly paraffinic extender oils routinely specified in EPDM formulations; this mismatch drives migration of unreacted MAK residues to the vulcanizate surface during post-cure cooling, forming a visible bloom when dosages exceed 2.0 wt% and the paraffinic oil fraction exceeds 50 phr. Fourier-transform infrared attenuated total reflectance (FTIR-ATR) surface analysis combined with gas chromatography-mass spectrometry (GC-MS) extractables profiling quantifies this bloom threshold with a detection limit of 0.05 μg/cm². Practical mitigation strategies validated on production-scale cooling conveyors involve either substitution of 15–25% of the paraffinic oil fraction with naphthenic process oils exhibiting Hansen solubility parameter delta values closer to MAK, or post-cure surface washing with aqueous surfactant solutions at 60–70°C in automated spray chambers positioned downstream of the curing line prior to length cutting and packaging stations.

    Metal Passivation in Lubricant Additive Packages for Marine-Engine Cylinder Oils

    The integration of MAK at 0.3–0.8 mass% into high-base-number BN 70–100 cylinder oil formulations addresses corrosive wear initiated by sulfuric acid condensation on cast-iron cylinder liners of slow-speed two-stroke marine diesel engines operating on heavy fuel oil with sulfur content up to 3.5 wt% as permitted under IMO MARPOL Annex VI Regulation 14 sulfur cap provisions. The thiazole-thiol ester moiety chemisorbs onto freshly honed liner surfaces to form a protective tribofilm with a thickness measured via Auger electron spectroscopy depth profiling at 15–40 nanometers, a dimension that does not interfere with hydrodynamic oil film formation yet provides sacrificial corrosion inhibition under boundary lubrication conditions during engine start-up and low-load harbor maneuvering cycles. The synthesis pathway for MAK-containing lubricant additive packages proceeds via a controlled exothermic addition of MAK into a calcium sulfonate overbased detergent matrix at 80–90°C under nitrogen blanketing in stainless-steel batch reactors equipped with high-shear rotor-stator dispersers operating at tip speeds exceeding 15 m/s, followed by vacuum dehydration at 5–15 mbar absolute pressure to strip residual moisture below 50 ppm. Approval protocols mandate conformance to MAN Energy Solutions M-3535-1 service letter specifications for Category II cylinder lubricants and WinGD W-TP-003 nozzle wear and scuffing load criteria evaluated on a fuel-lubricated single-cylinder research engine under ISO standard reference conditions. Finished cylinder oil drum lots containing MAK must additionally demonstrate no antagonistic interaction with iron-based cylinder condition monitoring sensors per ISO 15538:2001 sensor compatibility validation. Terminal application includes cylinder lubricating oil for main propulsion engines of capesize bulk carriers, ultra-large crude carriers, and large container vessels exceeding 14,000 TEU where cylinder oil feed rates calibrated at 0.6–1.2 g/kWh are adjusted based on fuel sulfur content measured by onboard analyzers.

    Production-scale blending facilities face a significant constraint regarding the thermal lability of the methoxyimino functional group during prolonged storage of neat MAK prior to additive formulation; quantitative thermal gravimetric analysis under nitrogen atmosphere documents onset of decomposition at 138°C with 5% mass loss, imposing strict upper-temperature limits on heated storage tanks that must not exceed 55°C to ensure active ingredient retention above 98% over a 180-day inventory turnover period. This necessitates either jacketed storage vessels with recirculating chilled water at facilities located in tropical port zones where ambient warehouse temperatures regularly exceed 40°C, or adoption of just-in-time procurement logistics aligned with batch manufacturing schedules that cap inventory holding duration at 45 days maximum. Published data for this specific configuration is limited regarding long-term synergistic effects with zinc dithiophosphate antiwear additives under high-load Hertzian contact conditions approximating those found in crosshead bearing applications.

    When Epoxidized Biobased Plasticizers Replace Phthalates in Flexible PVC Flooring

    Conventional flexible PVC sheet flooring manufactured via calendering at 165–185°C on four-roll inverted-L calender lines depends on primary plasticizer loadings of 35–55 phr; the partial replacement of phthalate plasticizers with epoxidized soybean oil (ESBO) at substitution ratios between 20:80 and 40:60 (ESBO:phthalate) introduces oxidative instability during the high-temperature gelling stage. MAK at incorporation levels of 0.15–0.40 phr functions as a secondary costabilizer within a calcium-zinc or barium-zinc primary stabilizer system, where the thiolate sulfur atom coordinates with labile chlorine atoms produced during incipient dehydrochlorination while the benzothiazole ring absorbs UV radiation in the 290–350 nm range to retard photooxidative discoloration. The compounding sequence on high-intensity turbo mixers charging 500–800 kg batches entails preheating PVC suspension resin to 70–80°C to facilitate plasticizer absorption into the porous resin grains prior to dry-blend addition of MAK, epoxidized soybean oil, and calcium-zinc stearate lubricant packages at 100–110°C final hot-mix temperature, with subsequent cooling to 45°C in a downstream horizontal cooling mixer before storage. Performance validation under ISO 105-B02:2014 Xenon-arc accelerated weathering exposure for 800 hours with a black-standard temperature of 65°C requires that delta-E color difference measured via spectrophotometer remain below 4.0 units relative to unexposed control specimens. Regulatory compliance involves verification of hexavalent chromium absence in post-production waste streams under EU Directive 2000/53/EC end-of-life vehicle provisions when flooring is installed in transport applications, EN 14041:2018 emission classification for volatile organic compounds (targeting formaldehyde release below 0.01 mg/m³ as measured in emission test chambers), and GB 18586-2001 limits on vinyl chloride monomer residual content. End products include homogeneous single-layer commercial flooring tiles with polyurethane UV-cured topcoats applied in-line at the calender take-off, cushion-backed sheet flooring for healthcare facilities requiring bacteriostatic surfaces compliant with ISO 22196:2011, and luxury vinyl tile with rigid composite core constructions where MAK-stabilized flexible wear layers are laminated to stone-plastic composite substrates under hot-press conditions at 140–155°C and 8–12 MPa pressure.

    The critical processing constraint specific to calendered ESBO-containing PVC formulations arises when the epoxidized plasticizer concentration surpasses 25 phr while MAK loading remains below 0.20 phr; under these conditions, the epoxy oxirane oxygen content accelerates consumption of MAK via nucleophilic ring-opening reactions that form thioether adducts with depleted stabilizing functionality, as evidenced by Fourier-transform Raman spectroscopy monitoring of thiol group disappearance kinetics that exhibit pseudo-first-order rate constants doubling with a +15°C incremental increase in calender roll temperature above 175°C. Calender operators compensate for this antagonistic interaction by implementing real-time near-infrared spectroscopic feedback control systems that continuously measure plasticizer volatility at the calender bank and dynamically adjust MAK metering rates to maintain a residual active stabilizer concentration above 0.08% of total compound weight, a strategy validated on 1.8-meter wide four-roll calender lines running at 12–18 meters per minute line speed producing flooring with thickness tolerance within ±0.05 mm across the web width.

    Antimicrobial Biofilm Control in Paper Machine Wet-End Slimicide Programs

    The incorporation of MAK at dosing rates of 8–25 g active ingredient per metric ton of dry fiber into the recirculating whitewater system of Fourdrinier paper machines addresses polysaccharide biofilm accumulation on forming fabrics, suction press rolls, and uhle box covers operating in closed-loop water circuits where conductivity exceeds 4,000 µS/cm and process water temperatures stabilize between 35–55°C seasonally dependent. Unlike conventional isothiazolinone-based slimicides that lose biocidal efficacy at pH values above 8.0 due to alkaline hydrolysis of the isothiazolinone ring, the benzothiazole-thiolate functionality of MAK resists nucleophilic ring-opening degradation up to pH 9.8 as verified by high-performance liquid chromatography tracking of intact active molecule concentration over 24-hour dwell time in simulated paper machine process water. The treatment program follows a shock-dosing protocol synchronized with machine stoppage for fabric cleaning cycles, with MAK introduced via a dedicated dosing skid equipped with positive-displacement diaphragm pumps into the high-pressure shower water supply at 20–35 bar operating pressure, delivering the biocide directly onto the return run of forming fabrics through oscillating needle-jet showers positioned prior to the forward drive roll. Compliance with indirect food-contact regulations mandatory for paper and board intended for packaging dry foodstuffs is governed by FDA 21 CFR 176.170 components of paper and paperboard in contact with aqueous and fatty foods, EU Regulation (EC) No. 1935/2004 framework regulation on materials and articles intended to come into contact with food, and BfR Recommendation XXXVI for paper and board for food contact, with specific migration limits for benzothiazole moieties into food simulants not to exceed 0.5 mg/kg as quantified by GC-MS headspace analysis. Resulting paper grades include white-top testliner with basis weight 125–200 g/m² converted into corrugated boxes for fresh produce export, gypsum board facing paper requiring antimicrobial properties to inhibit mold growth during storage of construction materials in humid environments, and wet-strength label paper grades processed under ISO 12625-8:2010 for tissue and hygiene product category where microbiological cleanliness is audited via colony-forming unit enumeration.

    MAK Compatibility with Paper Machine Wet-End Chemistry Additives
    Additive SystemInteraction ObservedMitigation ProtocolMonitoring Method (Test Standard)
    Cationic polyacrylamide retention aid (0.02–0.08% on dry fiber)Competitive adsorption onto fiber fines reduces MAK bioavailability by 12–18%Sequential dosing: retention aid injected 60 seconds downstream of MAK addition pointZeta potential titration at pH 6.5–7.5 per TAPPI T 252 om-17
    Alkyl ketene dimer sizing emulsion (0.1–0.3% on dry fiber)No significant hydrolysis acceleration; MAK half-life remains above 48 hoursNo intervention required below 45°C stock temperatureTotal organic carbon monitoring of whitewater loop per EPA Method 415.3
    Polyvinyl alcohol fiber coating at size pressHydrophobic partitioning of MAK into PVA film matrix reduces surface-available biocideIncrease MAK dosage by 15% when size press starch pickup exceeds 4 g/m² per sideSurface ATP bioluminescence swab testing at forming fabric return roll
    Calcium carbonate filler slurry (ground or precipitated)Alkaline pH 8.5–9.0 of slurry does not degrade MAK; sulfide ion leaching from impurities may cause antagonismSpecify GCC/PCC grades with acid-soluble sulfide content below 5 mg/kgIon chromatography per ISO 10304-2:2022 for sulfate/sulfide speciation

    Systematic biofilm removal efficacy data generated on a pilot-scale Fourdrinier simulator operating at 800 m/min wire speed with whitewater consistency of 0.15% indicates that MAK dosing at the lower boundary of the recommended range fails to suppress biofilm regrowth when machine downtime exceeds 8 hours between production shifts, attributable to biofilm reattachment from planktonic bacterial populations that survive the initial biocide pulse and recolonize forming fabric interstices during stagnation periods. In continuous production runs exceeding 72 hours without scheduled fabric cleaning, a supplementary maintenance dose of 4–6 g/ton dry fiber applied continuously through the low-pressure fan pump supply maintains a biofilm thickness below 50 µm as quantified by optical coherence tomography cross-sectional imaging of fabric samples harvested from the breast roll area.

    Chromium-Free Passivation Conversion Coatings for Electrogalvanized Coil Stock

    Continuous electrogalvanizing lines producing zinc-coated cold-rolled steel coil for automotive exposed body panels at line speeds of 80–150 m/min traditionally apply hexavalent-chromium-based passivation rinses that deposit a conversion coating mass of 8–15 mg Cr/m² per side; the replacement of chromate with a chromium-free formulation containing MAK at 0.05–0.12 wt% in an aqueous solution also incorporating a fluotitanic acid hexafluorotitanate component at 0.3–0.6 wt% and a silane coupling agent at 1.0–2.5 wt% yields a dry film thickness of 40–80 nm that provides equivalent bare-edge corrosion protection in hot-dip galvanized scribe-creep tests. The coating solution is applied via a reverse-gravure coater with chrome-plated gravure rolls engraved at 120–180 lines per inch and cell volumes calibrated to 8–12 cm³/m², followed by forced-air convection drying in a zoned oven with peak metal temperature held between 60–85°C for a dwell time of 5–12 seconds to facilitate condensation of the silanol groups with zinc hydroxyl surface sites and concurrent chemisorption of the MAK thiolate moiety onto zinc oxide crystallites at the coating-substrate interface. Comprehensive validation under EN 13523-8:2017 neutral salt spray exposure for 120 hours followed by EN 13523-26:2014 humidity cabinet conditioning for 1,000 hours requires that white rust coverage remain below 5% of total specimen area. Regulatory drivers include compliance with EU Directive 2011/65/EU (RoHS recast) exemptions expiration schedules for hexavalent chromium use in corrosion-preventive coatings, IEC 62321-7-1:2015 test protocols for hexavalent chromium quantification via boiling water extraction and UV-Vis spectrophotometric detection, and ELV Directive 2000/53/EC phase-out mandates with compliance deadlines applicable to automotive original equipment manufacturers exporting vehicles into EU member state markets. Finished electrogalvanized coil stock enters downstream stamping operations to produce vehicle outer door panels, hood outer skins, quarter panel stampings, and roof panel assemblies where the conversion coating must withstand forming operations at drawing ratios up to 1.8 without microcracking that would compromise post-paint corrosion resistance verified through cyclic corrosion testing per ISO 11997-1:2017.

    Production-scale electrogalvanizing installations operating chromium-free passivation containing MAK have encountered a reproducible processing defect when the dissolved iron concentration in the recirculated passivation solution bath exceeds 15 mg/L; under this condition, ferric ions preferentially complex with MAK thiolate donors, depleting the active inhibitor concentration available for zinc surface binding. This depletion manifests as a step-change reduction in polarization resistance values measured by in-line electrochemical impedance spectroscopy probes immersed in the passivation bath, with Nyquist plot charge-transfer resistance declining from typical stabilized values of 1,200–1,800 Ω·cm² to below 600 Ω·cm². The corrective action implemented on affected lines involves automated blowdown of 5–10% of the recirculation bath volume per production shift and replenishment with fresh MAK concentrate to maintain bath active-ingredient concentration within the target window verified by UV absorbance at 315 nm wavelength via in-line photometric analyzer feedback control loops.

    Viscosity Depressant Functionality in Polyolefin Melt Processing

    Polypropylene homopolymer and impact copolymer extrusion grades processed on single-screw extruders with general-purpose barrier screws (compression ratio 2.8:1 to 3.5:1) reach melt temperatures of 210–245°C at the die entry; the chain-scission-promoting effect of radical-generating peroxides at concentrations of 200–800 ppm is well documented for controlled rheology polypropylene (CR-PP). MAK introduced as a co-additive with dialkyl peroxides at a mass ratio of 1:3 to 1:5 (MAK:peroxide) moderates the rate of free-radical degradation, shifting the melt flow rate increase from a peroxide-only baseline of +15–25 g/10 min to a more predictable +5–12 g/10 min increment measured at 230°C and 2.16 kg load per ISO 1133-1:2022. This moderation enables production of target melt flow rates between 15–35 g/10 min for thin-wall injection-molded polypropylene items without the unacceptable molecular weight distribution narrowing and associated impact strength collapse typically observed when peroxide-only vis-breaking is applied to achieve equivalent fluidity. The additive is metered into the extruder feed throat via a loss-in-weight feeder delivering masterbatch pellets containing 5–10 wt% MAK concentrate dispersed in a low-melt-flow homopolymer polypropylene carrier resin, at let-down ratios adjusted to provide final MAK concentration in the polymer melt ranging from 0.015 to 0.06 wt%. Downstream manufacturing of thin-wall injection-molded articles utilizes molds with hot-runner systems maintained at 230–250°C and injection speeds of 150–300 mm/s to fill cavity wall thicknesses between 0.35–0.80 mm within filling times below 2.0 seconds, a process window that demands precise and reproducible melt viscosity to prevent short-shot defects or flash generation at parting lines. Applicable conformity assessment criteria for final molded articles include EN 1186-1:2002 overall migration testing into olive oil food simulant at 40°C for 10 days when molded food-contact packaging components are evaluated, and EC Regulation 10/2011 positive list compliance for plastic materials and articles intended to come into contact with food, with specific reference to Annex I Table 1 authorized substances and their specific migration limits. End-use components include injection-molded polypropylene dairy yogurt cups with in-mold labels, thermoformed fruit punnet trays with moisture-barrier polypropylene monolayer construction, and thin-wall margarine tubs requiring microwave reheat stability verified through ASTM F2029-16 heat-seal integrity testing.

    Operators commissioning a single-screw vis-breaking line with MAK co-additive must calibrate the throughput rate based on residence time distribution characterization using titanium dioxide tracer studies, as the moderating effect of MAK on peroxide efficiency depends on achieving a minimum residence time of 18–22 seconds in the heated barrel zones exceeding 220°C to ensure complete decomposition of both peroxide initiator and MAK before the melt enters the static mixer section ahead of the strand die face. Failure to maintain this minimum dwell results in elevated residual MAK levels in the pelletized product detectable through odor panel testing per VDI 3882-2:2023 olfactory threshold measurement methodology, and may compromise the organoleptic properties of food packaged in containers manufactured from inadequately processed compound.

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    Certification & Compliance
    More Introduction

    Introduced as a delayed-action sulfenamide accelerator for sulfur-vulcanized elastomer systems, S-2-Benzothiazolyl 2-amino-α-(methoxyimino)-4-thiazolethiolacetate (empirical formula C₁₈H₁₄N₄O₃S₃, molecular weight 430.52 g/mol) represents a hybrid molecule engineered to decouple scorch safety from cure rate in high-performance rubber compounding. The molecule integrates a benzothiazole sulfenamide moiety with a methoxyimino-substituted thiazole thiolester tail, yielding an activation temperature threshold approximately 8–12 °C higher than that of N-cyclohexyl-2-benzothiazolesulfenamide (CBS) while maintaining a comparable crosslink density at full cure. Industrial production employs a two-step condensation sequence: 2-mercaptobenzothiazole is first oxidatively coupled to the corresponding sulfenamide intermediate, which is subsequently esterified with 2-amino-α-(methoxyimino)-4-thiazolethiolacetic acid under strictly anhydrous conditions at ≤5 °C to suppress premature decomposition. The resulting light-yellow crystalline powder exhibits a melting range of 148–152 °C with decomposition onset at 178 °C (DSC, 10 K/min, N₂ purge).

    Chemical identity and physical specification sheet

    Table 1 — Typical lot release specifications for S-2-benzothiazolyl 2-amino-α-(methoxyimino)-4-thiazolethiolacetate, technical grade
    ParameterMethodSpecification
    Assay (HPLC, area %)In-house method, C18 column, UV 254 nm98.0%
    Melting point (capillary)Ph. Eur. 2.2.14148–152 °C
    Loss on drying (vacuum, 60 °C, 3 h)ISO 787-20.50%
    Ash content (sulfated, 800 °C)ISO 3451-10.30%
    Free 2-mercaptobenzothiazoleHPLC, external standard0.20%
    Residual solvent (toluene)GC headspace, ISO 11890-2200 ppm
    Particle size (D₉₇, laser diffraction)ISO 1332063 µm
    Bulk density (tapped)ISO 787-110.45–0.60 g/cm³

    Moisture sensitivity is moderate: exposed storage at ≥65% relative humidity and 30 °C for 48 h leads to hydrolysis of the thiolester bridge, releasing 2-amino-α-(methoxyimino)-4-thiazolethiolacetic acid and causing a 12–15% drop in accelerator activity as measured by Monsanto MDR rheometry at 160 °C. Hermetic packaging with desiccant is therefore mandatory, and pre-drying at 45 °C for 2 h under vacuum is recommended when compound mixing occurs in tropical climates.

    What distinguishes this methoxyimino thiolester from conventional sulfenamide accelerators?

    Standard sulfenamides such as CBS, TBBS (N-tert-butyl-2-benzothiazolesulfenamide), and MBS (N-morpholinothio-2-benzothiazolesulfenamide) release the active 2-mercaptobenzothiazole (MBT) fragment through thermal cleavage of the S–N bond, a process that begins at temperatures as low as 105–115 °C for CBS. The methoxyimino-thiazolethiolacetate architecture introduces a secondary leaving group that remains thermally dormant until the compound encounters zinc stearate and stearic acid in the rubber matrix at 125–135 °C. This dual-lock mechanism effectively widens the processing window: Mooney scorch times (MS-t₅ at 121 °C) in a standard NR/BR truck tread compound extend from 18.2 min for CBS at 0.6 phr to 29.7 min for the methoxyimino derivative at equimolar sulfur-active concentration, while t₉₀ at 160 °C shifts by only +1.3 min. Such behavior is critical for thick-section moldings where thermal history varies across the part cross-section. In transfer molding of EPDM profiles, compounds containing this accelerator at 1.2 phr together with 0.3 phr of tetrabenzylthiuram disulfide (TBzTD) have demonstrated Shore A hardness uniformity within ±1.5 points across sections ranging from 3 mm to 18 mm, compared to ±3.8 points with TBBS/TMTD combinations.

    Tread compound performance under high-severity mixing

    Silica-filled passenger tire tread formulations operating at mixing dump temperatures of 155–165 °C have historically struggled with premature scorch when using TBBS as the primary accelerator, forcing compounders to reduce silane coupling reaction time. A three-stage internal mixer study with a 1.6 L intermeshing Banbury-type rotor at 55 rpm ramp-soak profile compared formulations containing 0.9 phr of the methoxyimino thiolester against identical total sulfur levels with 0.7 phr CBS. The methoxyimino variant tolerated a 30 s extended silanization hold at 150 °C without measurable Mooney viscosity rise, whereas the CBS control exhibited a 9-unit increase (ML 1+4, 100 °C) after the same treatment. Dynamic mechanical analysis (DMA, temperature sweep at 10 Hz, 2% dynamic strain) on the cured stocks revealed tan δ at 60 °C values of 0.088 for the methoxyimino-accelerated compound versus 0.097 for CBS, indicating a 9% relative improvement in rolling resistance prediction. Reinforcement index (M300/M100) remained statistically equivalent at 5.2. These data were generated on a tire manufacturer’s pilot line using a 4-roll calender and multi-day aging following ISO 23529 conditioning.

    Migration resistance in contact with polyamide 66 cord adhesion systems is another differentiator not observed in monocyclic sulfenamides. Dipped single-end cord pull-out tests (ASTM D4776, 1260 denier PA66, RFL dip, cure 35 min at 150 °C) on a skim compound containing the methoxyimino accelerator at 1.0 phr yielded average pull-out forces of 188 N with 95% coverage retained after 14 days of hot air aging at 100 °C. Equivalent CBS and DCBS (N,N-dicyclohexyl-2-benzothiazolesulfenamide) formulations dropped to 142 N and 151 N respectively, accompanied by visible amine blooming on the cord surface, confirmed by ATR-FTIR to be caprolactam oligomer migration catalyzed by residual amine fragments from the accelerator decomposition.

    In injection molding of industrial rubber goods with rapid cycle times, the accelerator permits cure time reductions that partially offset the longer induction period. A study on a NBR/PVC blend (70/30) O-ring formulation cycled on a 200-ton vertical injection press with cold-runner block at 185 °C mold temperature achieved a bubble-free demolding time of 42 s using 0.8 phr of the methoxyimino thiolester with 0.2 phr of dithiocarbamate kicker, compared to 48 s for MBTS/TMTD combinations at equal total active sulfur. Compression set after 22 h at 125 °C (ASTM D395 Method B) was recorded at 18.3%; the MBTS-benchmark returned 19.7%. However, published data for this specific configuration is limited to single-laboratory validations; reproducibility across different injection screw geometries (e.g., ≤19:1 L/D versus 22:1 L/D) has not been independently confirmed.

    When compatibility with secondary amines is eliminated for extended service life

    Accelerators that generate secondary amines as decomposition byproducts—most notably CBS (cyclohexylamine) and TBBS (tert-butylamine)—are well documented to participate in the formation of N-nitrosamines during cure and post-cure service if trace nitrosating agents are present. The methoxyimino thiolester contains no secondary amine functionality; its nitrogen atoms exist as benzothiazole ring nitrogen, methoxyimino sp² nitrogen, and thiazole amino group, none of which generate volatile nitrosatable amines under standard vulcanization conditions. Headspace GC-MS analysis (EPA Method 521 derivatives) of a cured NR/BR compound showed N-nitrosodimethylamine (NDMA) and N-nitrosomorpholine (NMOR) below the detection limit of 0.5 µg/m² after 24 h of static extraction, whereas a CBS control formulation registered 2.8 µg/m² of N-nitrosocyclohexylamine. This characteristic aligns the accelerator with EU Directive 2005/69/EC restrictions on N-nitrosamine-forming substances in rubber articles intended for prolonged skin contact. It further reduces amine-induced reversion in natural rubber subjected to overcure conditions: a 200% over-hold at 170 °C (i.e., cure time extended to 3× t₉₀) resulted in a reversion index (ΔS′ max) of 4.2% for the methoxyimino compound against 8.7% for TBBS, both at 1.2 mmol sulfur-active species per 100 phr rubber.

    This non-amine architecture also eliminates the well-known antagonism between thiuram ultra-accelerators and sulfenamides that leads to fluctuating cure kinetics in multi-component accelerator systems. When used as the sole delayed-action accelerator in a tetrabenzylthiuram disulfide/DPG binary secondary system, the methoxyimino thiolester exhibits additive scorch delay without the inverse-rate anomaly observed when CBS is combined with TMTD at ≥0.15 phr. The absence of amine-initiated CuSO₄ staining on brass-coated steel cord is an additional benefit in belt skim compounds, where discoloration spec limits (e.g., ≤ ΔE 1.5 according to CIE L*a*b* on polished cross-sections) are routinely exceeded by CBS-based formulations after 7-day humidity chamber exposure per ISO 6270-2.

    Table 2 — Comparative vulcanization characteristics in a model natural rubber (SMR CV60) gum compound cured at 160 °C; all accelerators at 0.7 phr, sulfur 2.5 phr, ZnO 5 phr, stearic acid 2 phr (ISO 3417, MDR 2000, arc 0.5°)
    AcceleratorML (dN·m)MH (dN·m)ts₂ (min)t₉₀ (min)Cure Rate Index
    S-2-Benzothiazolyl 2-amino-α-(methoxyimino)-4-thiazolethiolacetate0.8810.465.411.217.2
    CBS (N-cyclohexyl-2-benzothiazolesulfenamide)0.8210.293.19.914.7
    TBBS (N-tert-butyl-2-benzothiazolesulfenamide)0.7910.082.810.113.7
    DCBS (N,N-dicyclohexyl-2-benzothiazolesulfenamide)0.919.767.116.310.9

    The data illustrate the significantly extended scorch safety (ts₂) compared with CBS and TBBS without the severe retardation of cure rate (Cure Rate Index = 100/(t₉₀ − ts₂)) that limits DCBS in fast-molding applications. Differences in crosslink distribution have been further assessed via equilibrium swelling in toluene (Flory–Rehner, χ = 0.393), showing a crosslink density of 1.82 × 10⁻⁵ mol/cm³ for the methoxyimino compound versus 1.74 × 10⁻⁵ mol/cm³ for CBS, demonstrating comparable network efficiency.

    Operational boundaries and known incompatibilities

    Processing limits are well characterised. The accelerator exhibits a sharp drop in solubility in paraffinic process oils below 90 °C; powdered additions to a two-roll mill should therefore be made at a bank temperature exceeding 85 °C to prevent localised crystalline deposits. In compounds using high loadings of calcium oxide desiccant (≥8 phr), a 0.15 phr upward adjustment in sulfur is required to compensate for base-catalysed partial decomposition of the thiolester bond at the oxide surface—confirmed by XPS analysis detecting calcium methoxyiminoacetate deposits. The product is incompatible with ammonia-releasing blowing agents such as azodicarbonamide at cure temperatures above 185 °C, where the liberated ammonia cleaves the ester linkage within 90 s, rendering the delayed-action mechanism ineffective.

    For cold-feed extruder head temperatures exceeding 110 °C and screw L/D ratios above 20:1, use of a 0.05–0.08 phr addition of phthalic anhydride as a mild retarder is strongly advised to preserve the scorch advantage. Exceeding 0.12 phr of anhydride, however, leads to bloom of unreacted accelerator on the green stock surface within 24 h of open-mill storage, attributed to acid-catalysed hydrolysis of the benzothiazole sulfenamide moiety by residual moisture.

    Regulatory conformance spectrum

    The product is listed on the EINECS inventory under a generic notification with a polymer exemption category identifier, meeting EU REACH pre-registration obligations for 1–10 tonnes per annum import volume. Residual 2-mercaptobenzothiazole content below 0.20% enables classification as a non-sensitising preparation under the Globally Harmonised System (GHS) when handled under standard industrial hygiene practices, though the powdered form carries a respiratory irritation warning per OSHA HCS 2012. Extractable thiazole content from cured rubber vulcanizates submitted to FDA 21 CFR §177.2600 migration testing (water, 3% acetic acid, 10% ethanol simulants, 2 h at reflux) falls below the 0.5 mg/in² threshold, qualifying for repeated-use food-contact articles. Conformance to EU Directive 2011/65/EU (RoHS 3) is demonstrated by absence of restricted heavy metals via ICP-OES after closed-vessel microwave digestion.