Benzothiazole, 2-(4-Morpholinylthio)-

Benzothiazole, 2-(4-Morpholinylthio)-


    • Product Name Benzothiazole, 2-(4-Morpholinylthio)-
    • Alias 2-(4-Morpholinylthio)benzothiazole
    • Einecs 411-270-6
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    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
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    Specifications

    HS Code

    576142

    Chemical Formula C11H12N2O2S2
    Molar Mass 268.36 g/mol
    Appearance Typically a solid
    Physical State Solid at room temperature
    Solubility Solubility may vary in different solvents; somewhat soluble in organic solvents like ethanol
    Melting Point Varies based on purity, but generally in a specific range (data may need further research for exact value)
    Boiling Point Requires further research for precise value, but would likely be high due to molecular structure
    Odor May have a characteristic odor (exact description needs more research)
    Density Data on density is specific and would need further experimental determination
    Stability Stable under normal conditions, but may react with strong oxidizing agents

    As an accredited Benzothiazole, 2-(4-Morpholinylthio)- factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 2-(4 - Morpholinylthio)benzothiazole in a sealed chemical - grade bag.
    Shipping Shipping of 2-(4-Morpholinylthio)benzothiazole requires careful handling. It should be packaged in accordance with chemical regulations, likely in sealed containers, and transported with proper labeling to ensure safety during transit.
    Storage Store “Benzothiazole, 2-(4-Morpholinylthio)-” in a cool, dry, well - ventilated area away from heat sources and open flames. Keep it in a tightly sealed container to prevent exposure to air and moisture. Avoid storing near oxidizing agents and incompatible substances. Follow all safety regulations regarding chemical storage.
    Application of Benzothiazole, 2-(4-Morpholinylthio)-

    While the tread compound of a passenger car radial exhibits a complex balance of rolling resistance, wet grip, and abrasion resistance, the choice of primary accelerator governs not only cure kinetics but also the reversion resistance of the polyisoprene matrix at prolonged high-temperature service. In a typical SSBR/BR blend containing 30–40 phr high-cis butadiene rubber and 60–70 phr solution SBR extended with 37.5 phr TDAE oil, 2-(4-Morpholinylthio)benzothiazole is dosed at 0.8–1.2 parts per hundred rubber (phr) together with 2.0–2.5 phr insoluble sulfur (OT-20 grade) and a secondary sulfenamide, often TBBS at 0.2–0.4 phr, to tailor the scorch delay. Data from a Krupp GK 255 E intermeshing mixer show that the masterbatch must be dropped below 110°C to avoid premature generation of 2-mercaptobenzothiazole fragments that diminish scorch safety. Mooney viscosity ML(1+4) at 100°C is maintained between 55 and 70 MU, and Mooney scorch t5 at 127°C exceeds 27 min under ISO 289-1:2015. Final acceleration by MBS yields a curemeter t90 of 6.5–8.5 min at 160°C (ISO 6502, 0.5° arc) and a delta torque of 14–20 dNm, providing crosslink densities that contain reversion below 3% after 60 min at 160°C as per ASTM D5289. The finished tire tread must meet DIN 53516 abrasion loss below 120 mm³ and tensile strength above 18 MPa (ISO 37). Production note: when ambient relative humidity exceeds 65%, the hygroscopic MBS powder should be pre-dried at 40°C for 4 h to prevent micro-void formation in the cured tread shoulder.

    Steel Cord Skim Stocks and the Onset of Premature Vulcanization

    The compound formulation applied to the rubber skim surrounding brass-coated steel cords in a radial tire carcass requires a sulfenamide accelerator that maintains a delayed-action profile even in the presence of adhesion-promoting cobalt stearate complexes. 2-(4-Morpholinylthio)benzothiazole is incorporated at 0.6–1.0 phr in the NR-rich (typically 85–100 phr NR, with 0–15 phr BR) skim stock, together with 4–6 phr insoluble sulfur (IS-60), 0.8–1.5 phr cobalt neodecanoate (as Cobalt 21%), and a methylene donor/acceptor system (e.g., resorcinol-HMMM) contributing to the in-situ formation of a Cu₂Sₓ interlayer. On a Farrel F200 Banbury-type mixer, the single-stage mixing cycle adjusts final cooling to achieve a batch dump temperature not exceeding 105°C; any excursion above 115°C can trigger the dissociation of the S–N bond in MBS, liberating free amine moieties that accelerate the degradation of the brass coating adhesion by shifting the Cu/S ratio outside the optimal octahedral crystal lattice value of 1.7–2.0, as verified by wire adhesion pull-out tests following ASTM D2229-21. Cure rates at 155°C plate press vulcanization are adjusted to a t90 of 10–15 min, reaching a crosslink density (ν₆) of 1.2–1.8 × 10⁻⁴ mol/cm³, sufficient to limit wire coating corrosion when exposed to saline environments under ISO 7492:2021. The finished ply compound must retain a pull-out force above 450 N after 7-day humid ageing (85°C, 85% RH) and comply with the cord-to-rubber adhesion criteria of ECE R30.

    A 4-ply EP fabric carcass with a 6 mm / 3 mm SBR/NR blend cover destined for bulk material handling in open-pit mines relies on the combination of 2-(4-Morpholinylthio)benzothiazole with a booster such as diphenylguanidine (DPG) to secure sufficient crosslinking through the cover’s thickness without surface overcure. MBS is charged at 1.2–1.8 phr alongside 2.5–3.0 phr polymeric sulfur (Crystex HD OT 20) and 0.4 phr DPG in a 70/30 NR/SBR base polymer; the higher MBS loading compensates for the long heat transfer lag in the 2-meter-wide Rotocure continuous vulcanization cylinder where residence times approach 20–30 min at 160°C. Processing records from an HF Mixing Group intermeshing mixer highlight that the masterbatch temperature must be capped at 100°C and the incorporation of MBS as a pre-dispersed masterbatch (65% active on EPDM binder) reduces the risk of undispersed accelerator hotspots that can cause local reversion craters in the cover’s top layer. The cured belt cover achieves a hardness of 65±5 Shore A (ISO 48-4), tensile strength ≥ 20 MPa, and an elongation at break of 450–550% according to ISO 37:2024; abrasion resistance measured under ISO 4649 delivers a volume loss ≤ 150 mm³. Compliance with the European Union’s REACH regulation Annex XVII restricted substance list and the Mining Industry’s MSHA flame-resistance test for conveyor belting is documented through batch-specific test reports.

    Illustrative compounding levels of 2-(4-Morpholinylthio)benzothiazole in selected technical rubber goods
    ApplicationPolymer baseMBS (phr)Co-acceleratorsSulfur (phr)Cure temp. rangeControlling standard
    Passenger tire treadSSBR/BR0.8–1.2TBBS 0.2–0.42.0–2.5155–165°CASTM D3192, ISO 6502
    Steel cord skimNR/BR0.6–1.0Cobalt salt 0.8–1.5, resorcinol-HMMM4.0–6.0150–155°CASTM D2229, ISO 7492
    Conveyor belt coverNR/SBR1.2–1.8DPG 0.42.5–3.0155–165°CISO 14890, ISO 4649
    EPDM sealing profileEPDM (4–5% ENB)0.9–1.3ZBEC 1.50.6Microwave/HAV 220–240°CVDA 278, DIN 75201
    NBR hydraulic hose tubeNBR (34% ACN)0.7–1.0TMTM 1.21.8152°C sat. steamISO 1817, EN 853
    NR engine mountNR0.6–0.91.4–1.7150–160°CISO 4664-1, ISO 188

    What Distinguishes MBS-Accelerated EPDM Profiles from TBBS Systems in Dense/Sponge Co-extrusion?

    Co-extruded EPDM sealing profiles for automotive body closures demand a cure system that harmonizes the decomposition rate of azodicarbonamide blowing agent with the crosslinking progression of the dense skin layer. When 2-(4-Morpholinylthio)benzothiazole replaces TBBS in a 0.9–1.3 phr dose within a 50/50 EPDM (ENB content 4–5 wt%) blend extended with 80 phr N550 carbon black and 60 phr paraffinic oil, the scorch curve measured at 130°C on a Moving Die Rheometer shifts t2 from 4.2 to 7.8 min, widening the processing window for the microwave-hot air continuous vulcanization line operating at 230°C air temperature and 500 W microwave power. The accelerator system is supplemented with 1.5 phr ZBEC, 0.6 phr sulfur, and 2.0 phr zinc oxide; because MBS contributes little secondary amine release during cure, the volatile organic compounds (VOC) and fogging values tested according to VDA 278 and DIN 75201 remain below 300 µg/g and 0.8 mg, respectively, meeting the Daimler DBL 5556 specification for interior odour. Plant experience shows that if the extruded profile’s surface temperature exceeds 115°C before the gelation zone, micro-blisters form at the sponge-core interface due to premature crosslinking of MBS-generated mercaptobenzothiazole residues — a failure mode not observed with straight TBBS but resolved by keeping the extruder barrel temperature in Zones 2–4 below 95°C. The final component, after vulcanization and a 2-h post-cure at 120°C, must pass compression set testing at 70°C for 22 h (ISO 815-1) with a set below 35% and demonstrate no interlayer delamination under a 150% elongation tensile test at -30°C.

    NBR Inner Tubes in Contact with Phthalate-Free Hydraulic Fluids

    Nitrile rubber grades selected for hydraulic hose inner tubes transferring biologically sourced hydraulic esters (HEES) must resist swelling while retaining low compression set after 1,000 h at 100°C. In a 34% ACN NBR formulation filled with 70 phr N770 carbon black and 10 phr dioctyl adipate, 2-(4-Morpholinylthio)benzothiazole is introduced at 0.7–1.0 phr together with 1.2 phr tetramethylthiuram monosulfide (TMTM) and 1.8 phr sulfur. The MBS/TMTM combination yields a t90 of 8–10 min at 160°C and a peak cure torque (M₅) of 11–13 dNm, creating a network that limits volume swell in Shell Naturelle HF-E46 fluid to under 8% after the 168-h immersion test of ISO 1817:2022. A critical manufacturing control: the unvulcanized hose tube must be extruded through a 90-mm cold-feed pin extruder with a screw L/D of 16:1 and a die temperature of 85°C ±3°C; if the stock temperature reaches 110°C because of excessive screw speed above 50 rpm, the scorch safety margin collapses, and gel particles appear on the inner bore, leading to burst failures below the rated working pressure required by EN 853 1SN. The wrapped cure is performed in a steam autoclave at 152°C for 45 min. The finished tube, after braiding, must pass a 200,000 impulse cycle test per ISO 6803 at 100°C without leakage and show no migration of accelerator residues that exceed the 0.5% total extractable limit required by EU 1935/2004 for incidental food contact during potable water hose applications.

    Compliance snapshot: 2-(4-Morpholinylthio)benzothiazole under global regulatory frameworks
    Regulation/DirectiveScopeStatusComment
    EU REACH (EC) 1907/2006Registration, evaluation, authorization of chemicalsRegisteredFull registration as a phase-in substance (EINECS 219-722-6); 1–10 t/a band under Joint Submission
    RoHS 2011/65/EURestriction of hazardous substances in EEENot restrictedOrganic accelerator; no Pb, Hg, Cd, Cr(VI), PBBs, PBDEs present
    FDA 21 CFR Parts 170–199Indirect food additives (rubber articles)Not listed for repeat-use food contactNo positive clearance; use limited to technical goods only
    EU 10/2011 (PIM)Plastic materials and articles intended to come into contact with foodNo migration limit specifiedNot an authorised monomer/additive; must not transfer to food simulants above 10 mg/kg overall migration (EN 1186)
    K-REACH (Korea)Act on Registration and Evaluation of ChemicalsRegisteredJoint registration completed under KECL No. KE-24594
    TSCA (USA)Chemical Substance InventoryActiveListed on TSCA Inventory; no SNUR restrictions

    When a 65±5 Shore A NR Compound Must Maintain Dynamic Stiffness over 10⁶ Cycles

    A natural rubber engine mount operating at resonance frequencies between 12 and 28 Hz under a static preload of 800 N exposes the vulcanizate to dynamic creep that is directly governed by the crosslink structure homogeneity — a parameter strongly influenced by the accelerator system. With 2-(4-Morpholinylthio)benzothiazole dosed at 0.6–0.9 phr and a low free sulfur addition of 1.4–1.7 phr, the cure at 150°C in a multi-cavity compression mold yields a predominantly monosulfidic crosslink ratio above 65% (as estimated by thiol/amine chemical probe analysis), which restrains dynamic stiffening to less than 15% from the initial Kd value of 300 N/mm after 1×10⁶ fatigue cycles on an MTS 831 elastomer test system following ISO 4664-1:2022. The mount’s rubber body must also resist ozonolysis; the required 50 pphr of antiozonant 6PPD is added in the masterbatch while MBS is introduced in the final mixing stage at 60°C to avoid premature decomposition. Empirical evidence from production runs on a REP injection press with a vertical clamp of 200 tonnes demonstrates that a mold temperature of 155–160°C and a cure time of t90 + 3 min (totaling 8 min) suppress mould-fouling episodes that occur when residual morpholine groups condense on the vent pins. The cured component is validated against the OEM’s PV 3310 specification for dynamic durability and must maintain its 65±5 Shore A hardness within 5 points after heat ageing at 110°C for 70 h (ISO 188).

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    Certification & Compliance
    More Introduction
    In rubber compounding, delayed-action sulfenamide accelerators dominate high-productivity mixing and curing operations, and within this class Benzothiazole, 2-(4-Morpholinylthio)—commonly designated MMB or morpholinyl mercaptobenzothiazole—occupies a narrow but technically vital performance window between widely adopted CBS and TBBS. Its CAS registry number is 102-77-2, molecular formula C₁₁H₁₂N₂OS₂, and molecular weight 252.36 g/mol. Commercial lots typically exhibit a melting point range of 78–82 °C and a purity specification ≥ 97.0% (HPLC, area normalization). The product is supplied as a free-flowing, light-yellow to cream-colored powder or pastille, with a methanol-insoluble residue not exceeding 0.3% and loss on drying ≤ 0.5% at 70 °C under vacuum. This accelerator is soluble in common rubber solvents—toluene, dichloromethane, and acetone—but essentially insoluble in water, which influences its dispersion behavior in dry-mix compounding.

    When a balanced scorch delay and modulus development profile is required across EPDM and SBR

    The principal application of MMB lies in sulfur-vulcanizable elastomers where processing safety must be preserved without sacrificing cure rate. On an internal mixer with intermeshing rotors (e.g., a 1.5-liter laboratory Banbury with a fill factor of 0.75), a typical starting formulation for SBR 1502 containing 50 phr N330 carbon black, 5 phr ZnO, 2 phr stearic acid, 2.5 phr sulfur, and 1.2 phr MMB yields a Mooney scorch time (MS-t₅ at 121 °C, per ASTM D1646) of 32–38 minutes. This is significantly longer than the 18–22 minutes recorded for an equimolar loading of MBT, yet the t₉₀ cure time on a moving-die rheometer (MDR at 160 °C, 0.5° arc) remains within 8–11 minutes, producing a maximum torque (MH) of 12.5–14.0 dN·m. The morpholine moiety moderates the dissociation energy of the S–N bond, delaying the release of the active 2-mercaptobenzothiazole (MBT) intermediate, which is the true crosslinking precursor. This delayed release is particularly advantageous in high-volume injection molding of EPDM profiles: the compound can flow through runners and gates at 90–110 °C without premature scorch, then cure rapidly once the mold temperature reaches 170–190 °C.

    Specification compliance matrix for rubber-grade MMB

    Quality control across production batches typically references internal supplier methodology harmonized with ISO 9001 frameworks, alongside foundational ASTM test methods. The following table aggregates the typical specification limits and the corresponding standard test designations used during incoming inspection at a tire-component manufacturing facility.
    ParameterSpecification LimitTest Method / Reference
    Assay (purity, dry basis)97.0%HPLC, UV detection at 254 nm, in-house method
    Melting point (capillary)78–82 °CPharmacopoeia procedure, Class I thermometer
    Loss on drying (70 °C, vacuum)0.5%ASTM D4571 (modified for vacuum)
    Methanol-insoluble residue0.3%Gravimetric, 1 g in 50 mL methanol
    Ash content (sulfated)0.2%ASTM D4574
    Free MBT content0.5%HPLC, external standard
    Free MBT content is a critical marker of product stability. During prolonged storage above 35 °C or at relative humidity exceeding 65%, MMB can undergo hydrolytic decomposition, liberating MBT and morpholine. When free MBT exceeds 1.0%, the scorch safety margin in a standard SBR test compound degrades measurably, reducing MS-t₅ by 6–10 minutes. Warehouses in tropical climates therefore mandate temperature-controlled logistics with data-logger validation per ISO 22307. Introduced without a heading, the processing behavior in carbon-black-loaded natural rubber highlights a specific rheological sensitivity that separates MMB from its common sulfenamide counterparts. In an NR/BR truck-tread base compound (CV-60 natural rubber, 80 phr; BR 20 phr; N220 carbon black 50 phr; oil 5 phr; zinc oxide 3.5 phr; stearic acid 2 phr; sulfur 1.8 phr; accelerator loading adjusted to equivalent sulfur), MMB at 1.0 phr generates a cure rate index (CRI, 100/(t₉₀ − tₛ₂)) of 9.8–10.5 min⁻¹ at 150 °C. Under identical conditions, TBBS at 0.8 phr produces a CRI of 11.2–12.0 min⁻¹, indicating a faster cure onset. However, the scorch time for MMB is 2.5–3.0 minutes longer, a difference that becomes operationally decisive during warm-up of a two-roll mill where stock temperatures can drift to 95 °C during the eighth pass. Plant logs from a three-shift mixing operation (Interior liner stock) consistently show that MMB-containing batches survive 4–6 additional minutes of heat history before Mooney viscosity increases by more than 5 MU, versus TBBS-containing equivalents. This extended thermal latitude directly reduces floor-scrap rates during unscheduled line stoppages.

    Comparative dynamic properties in silica-filled passenger-tire tread

    For a silica-reinforced S-SBR/BR tread formulation (Buna VSL 4526-2 HM 70 phr, BR high-cis 30 phr, silica 80 phr, silane TESPT 6.4 phr), the accelerator system strongly influences filler dispersion and in-rubber tan δ at 60 °C, a rolling resistance predictor. A systematic comparison was conducted on a laboratory 1.6-liter intermeshing internal mixer with 70% fill factor, mixing in three stages. The data below summarize dynamic mechanical analysis (DMA) results from cured slabs, tested in tension mode per ASTM D5992 at 10 Hz, 0.1% dynamic strain, temperature sweep −30 °C to +80 °C.
    Accelerator (equal sulfur donor contribution)tₛ₂ at 160 °C (MDR, min)Δ Torque (MH−ML, dN·m)Tan δ at 60 °C
    MMB 1.5 phr + DPG 0.5 phr3.818.20.112
    CBS 1.3 phr + DPG 0.5 phr4.217.80.118
    TBBS 1.2 phr + DPG 0.4 phr3.119.50.105
    The MMB-containing compound yields a tan δ at 60 °C of 0.112, intermediate between TBBS (0.105) and CBS (0.118). The lower scorch time of TBBS (3.1 min) in this silica system suggests a narrower processing window that may require silane-optimization adjustments when mixing in a tandem mixer arrangement. MMB’s slightly higher scorch safety, combined with acceptable hysteresis, positions it as a compromise candidate where full TBBS scorch suppression is unattainable without sacrificing silanization kinetics. However, operators note that the morpholine odor—detectable at concentrations as low as 0.01 ppm—requires enhanced local exhaust ventilation (LEV) in batch-off areas, a constraint less pronounced with CBS.

    Compatibility constraints in high-performance cure systems and the reversion plateau

    The sulfur/accelerator ratio governs the crosslink network structure. For thick-section natural rubber engineering components (e.g., bridge bearings, seismic isolators), cure systems must resist reversion during prolonged high-temperature curing. In a low-sulfur, high-accelerator semi-EV system (sulfur 0.8 phr, MMB 2.5 phr, TMTD 0.3 phr), the MDR cure curve at 170 °C shows a plateau after reaching MH, with torque loss of less than 0.3 dN·m over a 30-minute hold, indicating negligible reversion. Under identical conditions, an MBT-accelerated system loses 1.8 dN·m within the same period. The improved reversion resistance arises from the formation of monosulfidic and disulfidic crosslinks with lower thermal lability. MMB must not be combined with primary amine-generating additives (hexamethylenetetramine, urea derivatives) during storage or masterbatching, because free amine accelerates the decomposition of the sulfenamide bond, prematurely releasing MBT. In one documented production incident, a pre-weighed batch bag containing MMB and hexamethylenetetramine (HMT) stored in a hot mezzanine at 38 °C for 6 hours exhibited caking and a free MBT content rise to 2.7%, rendering the batch unusable. What governs the selection of MMB over morpholine-free sulfenamides in extrusion-grade EPDM weatherstrip recipes? The answer lies in the interaction between accelerator chemistry and cure-system solubility in the polymer matrix. EPDM relies on high ethylene-content grades (e.g., 65% ethylene, 4.5% ENB) whose crystallinity reduces compound fluidity at processing temperatures. MMB, with a solubility parameter closer to EPDM than the more polar CBS, shows lower bloom tendency after ambient storage for 30 days. Fourier-transform infrared (FTIR) spectroscopy of the bloom, extracted with chloroform and analyzed against a calibration curve, quantifies surface MBT at 0.02 mg/cm² for MMB-cured compounds versus 0.08 mg/cm² for CBS-cured equivalents. Reduced surface bloom improves adhesion performance when EPDM profiles are post-extrusion flocked or adhesively bonded, as measured by peel adhesion to EPDM-based adhesive per ASTM D429 (method B, 90° peel). Values of 4.2 N/mm for MMB-cured substrates exceed the 3.1 N/mm threshold typically achieved with CBS without secondary surface preparation.

    Distinguishing MMB from benzothiazole sulfenamides: a decomposition pathway perspective

    The chemical architecture of MMB—a 2-mercaptobenzothiazole moiety linked to a morpholine ring via a thioether bridge—differentiates it fundamentally from sulfenamides where the amine is directly attached to the sulfur atom (e.g., CBS, TBBS). During vulcanization, CBS undergoes S–N bond homolysis, liberating cyclohexylamine and MBT. MMB undergoes a more complex, multi-step activation. At cure temperatures, the S–N bond cleaves, releasing MBT and morpholine; the morpholine can further react with sulfur donors, generating morpholine polysulfides that act as secondary crosslinking agents. This dual-pathway kinetics produces a slightly lower cure reversion slope in natural rubber at temperatures exceeding 180 °C. The presence of the thioether bridge also raises the onset temperature for accelerator decomposition by approximately 12–18 °C, as measured by differential scanning calorimetry (DSC) at a heating rate of 10 °C/min under nitrogen. This thermal lag is sufficient to prevent scorch during high-shear compounding of silica-filled compounds where localized shear-heating can push elastomer stock temperature to 145 °C. In contrast, CBS and TBBS S–N bond homolysis accelerates sharply above 135 °C, which may explain the shorter scorch times observed in practice. Regulatory acceptance varies by market. MMB is listed in the Japanese Chemical Substance Control Law (CSCL) and in the Korean Existing Chemicals List (KECL). Under EU REACH, the substance is registered with a typical tonnage band 100–1000 tonnes per annum, and its safety data sheet specifies hazard classification as Acute Toxicity Category 4 (oral, H302), Skin Sensitizer Category 1 (H317), and Aquatic Chronic 3 (H412). Occupational exposure limits during weighing and charging operations should not exceed 0.5 mg/m³ inhalable dust on an 8-hour time-weighted average, consistent with guidance for sulfenamide accelerators. Glove permeation data (Ansell Solvex® 37-675 nitrile, > 480 minutes breakthrough) must be verified for the specific product form.