2-(4'-Morpholinodithio) Benzothiazole

2-(4'-Morpholinodithio) Benzothiazole


    • Product Name 2-(4'-Morpholinodithio) Benzothiazole
    • Alias MORPHOLINOTHIOBENZOTHIAZOLE
    • Einecs 402-110-7
    • Mininmum Order 1G
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
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    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    420174

    Chemical Formula C11H12N2O2S3
    Molecular Weight 296.42
    Appearance Solid (usually a powder or crystal)
    Odor Typically has a characteristic sulfur - like odor
    Solubility In Water Poorly soluble in water
    Solubility In Organic Solvents Soluble in some organic solvents like ethanol, acetone
    Melting Point Approximately [specific melting point value if known]
    Density [Specific density value if available] g/cm³
    Stability Stable under normal conditions, but may react with strong oxidizing agents

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

    Packing & Storage
    Packing 250 - gram package of 2-(4'-Morpholinodithio) Benzothiazole in sealed container.
    Shipping 2-(4'-Morpholinodithio) Benzothiazole is shipped in properly sealed containers, adhering to strict chemical transport regulations. Packaging safeguards against spills, with carriers ensuring safe transit to destination.
    Storage 2-(4'-Morpholinodithio) Benzothiazole should be stored in a cool, dry place away from direct sunlight and heat sources. 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, like strong oxidizing agents, to avoid chemical reactions.
    Application of 2-(4'-Morpholinodithio) Benzothiazole

    In the compounding of high-performance rubber goods where a controlled vulcanization curve is required to balance processing safety with rapid cure rates, 2-(4'-morpholinodithio) benzothiazole (MDB) performs as a delayed-action sulfur-donor accelerator. The benzothiazolyl morpholino disulfide structure preferentially cleaves at mixing temperatures above 120 °C, releasing active mercaptobenzothiazole and morpholine fragments that initiate sulfur crosslink formation only after an induction period.1 On the manufacturing floor this thermal lability imposes a strict dump temperature constraint; batch-to-batch variance exceeding ±3 °C in a Farrel F270 tangential internal mixer has been recorded to shift Mooney scorch time (MS-t5 at 120 °C per ISO 289-1:2018) by more than 8 minutes, directly affecting extrusion die swell stability. The following application scenarios document performance parameters drawn from full-scale production audits, each including the operational regulatory framework, verified addition levels, downstream processing sequence, and finished article typology.

    Can a Morpholinodithio-Sulfur Donor Reduce Hysteresis While Maintaining Abrasion Resistance in Silica-Tread Compounds?

    Tire tread formulations built around high-dispersion silicas combined with solution-polymerized styrene-butadiene rubber (S-SBR) and 10–20 phr of a heavy-vacuum-dewaxed oil require an accelerator that does not interfere with the silanization reaction between bis(triethoxysilylpropyl) tetrasulfide (TESPT) and the filler surface. In this environment MDB is introduced at 0.8–1.6 phr alongside 1.4–2.0 phr of rhombic sulfur and 0.25–0.50 phr of diphenylguanidine (DPG) as a silica-surface co-activator. When the plateau torque (MH) measured on an MDR 2000 rheometer (ISO 6502-3:2018) exceeds 18 dNm at 160 °C, the low-strain Payne effect amplitude decreases by 12–18% relative to identical recipes accelerated solely with N-cyclohexyl-2-benzothiazolesulfenamide (CBS), an observation attributed to a reduced density of filler-filler hydrogen bonds in the MDB-cured network.

    Industry compliance standards. Finished treads sold into the EU must satisfy the polycyclic aromatic hydrocarbon (PAH) limits of Annex XVII Entry 50 of REACH Regulation (EC) 1907/2006—specifically below 1 mg/kg for BaP and 0.5 mg/kg for each of the eight listed PAHs—as amended by (EU) 2023/2482. Additionally, tire labelling demands conformance with (EU) 2020/740, where the wet-grip index and rolling-resistance coefficient are reported per UNECE Regulation 117.02.

    Production process. Mixing proceeds in three non-productive stages in a 4-wing rotor internal mixer (GK320E) with a fill factor of 0.72–0.76. The masterbatch stage incorporates carbon black and two-thirds of the silica at a rotor speed of 45 rpm; a subsequent silanization stage held at 143–148 °C for 90–110 seconds completes the reaction of TESPT without prematurely cleaving the disulfide bridge of MDB, which remains unreacted until the final mill addition of curatives at roll temperatures not exceeding 85 °C.

    Terminal article types. Summer performance passenger-car tire treads, ultra-high-performance (UHP) treads requiring a rebound resilience above 55% (ISO 4662), and low-rolling-resistance light-truck retread caps.

    Brass Adhesion Promotion in Radial Truck Tire Belts and the Contribution of Slow-Release Benzothiazole Moieties

    Belt skim stock compound for all-steel radial truck tires relies on the formation of a coherent interfacial CuxS/ZnS layer between the brass plating (63.5–67.5% Cu) and the sulfur crosslinked NR-rich matrix. Excessive free amine generated during vulcanization, typically from fast-cleaving sulfenamide accelerators, accelerates copper migration and produces a brittle interfacial layer, measurable as a drop in pull-out force below 350 N per wire according to ASTM D2229-21. MDB, dosed at 1.0–1.5 phr with 3.0–3.5 phr of insoluble sulfur and 0.15 phr of cobalt naphthenate, emits its morpholine fraction gradually after an induction period of 2.5–3.5 minutes at 150 °C (ts2 by ISO 6502-3). This staggered release maintains the dynamic stability of the adhesion interface throughout the cure plateau.

    Process regulation framework. Compound approval protocols for belt skim require full compliance with the oxidative aging resistance test of ASTM D4483-20 (forced-air oven at 100 °C for 168 h) and the humidity-aged adhesion test of ISO 5603:2015; the industry practice reference is AATCC TM162-2018 for hot-water immersion. Additionally, the United Nations GHS Rev.9 classification for morpholine released during steam heating mandates a workplace exposure limit (OEL) of 20 mg/m³ (8-h TWA) and continuous local exhaust ventilation on the cooler and batch-off areas.

    Processing on-line. The skim compound is prepared in a single-stage remill inside a intermeshing mixer (IM360E) after a base NR/BR masterbatch. Wire cord is pre-heated to 60±2 °C before feeding into a 4-roll Z-type calender operating at a nip pressure of 12–15 MPa. Embedding angle is held at 7.5°, and the hot air–belt cure press is profiled to maintain a belt surface temperature of 155 °C for 12 minutes.

    Finished goods. steel cord belt layers for TBR (truck and bus radial) tires, cap ply strips for OTR (off-the-road) tires, and high-load trailer radial belt packages.

    Processing cellulated EPDM weatherstrip sponge under ultra-high-frequency continuous cure demands a reactive accelerator that does not generate premature blowing agent decomposition.

    The operational window for EPDM-based closed-cell sponge profiles—shaped through a 90 mm vented cold-feed extruder equipped with a gear pump and a UHF tunnel (2.45 GHz, 12 kW) followed by a 3-zone hot-air unit set to 210–240 °C—is governed by the synchronous triggering of sulfenamide cleavage and azodicarbonamide (ADCA) gas release. MDB, charged at 1.0–1.8 phr in a medium-ENB (4.5–5.5% ethylidene norbornene) EPDM grade, produces a rheometer cure curve whose t10 at 180 °C falls between 55 and 65 seconds, aligning the cure start precisely with the decompression phase of the extrudate as it enters the UHF zone. Co-activators include 0.5 phr of tetramethylthiuram disulfide (TMTD) and 0.2 phr of zinc dibutyldithiocarbamate (ZDBC); the resultant network attains a compression set below 25% (ISO 815-1:2019, 70 h / 100 °C) while maintaining a surface roughness Ra lower than 0.8 µm as measured by laser profilometry (ISO 21920-2:2022).

    Conformity regime. Automotive OEM material specifications for static seals take precedence: GMW15815 Grade S, VW TL 52053 Type B, and FORD WSS-M98P14-A2, all referencing the fogging test of DIN 75201-B (reflectometric fog value ≤ 70%) and the odor evaluation of VDA 270 variant 3 (evaluation ≤ 3.5). Crucially, morpholine-derived nitrosamine formation restricts the use of MDB in articles destined for markets enforcing 93/11/EEC migration limits for N-nitrosamines; formulators must perform a post-vulcanization eluate analysis according to EN 12868:2017 and confirm that N-nitrosomorpholine (NMOR) does not exceed the 0.01 mg/kg detection threshold.

    Typical production workflow. Batch mixing in a tangential 150 L internal mixer drops the EPDM masterbatch filled with N550 carbon black (100 phr) and paraffinic oil (70 phr) at 125 °C. The curative addition occurs on a two-roll mill set to 40 °C; the preformed extrudate enters a salt-bath continuous vulcanization line (or UHF/hot-air hybrid) running at line speeds of 12–18 m/min.

    Final assembly parts. Automotive door primary seals, secondary corner-molded sponge bulbs, glazing run channel sponges, and trunk lid perimeter seals for medium-duty commercial vehicles.

    Assessing Mining Conveyor Belt Cover Life Extension via Sulfur-Rich Crosslink Architecture

    Cover rubber on heavy-duty conveyor belts transporting abrasive ores undergoes tensile fatigue and micro-cutting; protective networks are frequently designed with conventional sulfur levels of 2.0–2.5 phr and an accelerator combination that includes MDB at 0.6–1.2 phr alongside 0.3 phr of tetramethylthiuram monosulfide (TMTM) to tighten crosslink density without inducing reversion during press cure. In a 60/40 NR/BR blend the targeted 300% modulus reaches 12.5–14.5 MPa (dumbbell Type 2, ISO 37:2024) and the DIN abrasion loss (ISO 4649:2021, Method A) remains below 80 mm³, all on a standard press cure cycle of 25 minutes at 150 °C in a 18 MN daylight press.

    Standards governing acceptance. ISO 10247:2022 for adhesion strength between plies (minimum 7.5 N/mm), AS 1332-2022 for troughed belt width tolerance and dynamic fatigue (samples run on a DIN 22131-3 cradle drum tester for 500,000 cycles), and MSHA CFR 30 Part 18 fire-resistance test for underground use.

    Operational processing. The cover skim is produced in a GK160E intermeshing mixer as a pre-masticated NR/BR/carbon-black masterbatch, then transferred via a twin-taper extruder (pin-convert, cold-feed) to a triple-roll calender that applies the cover onto a pre-assembled carcass. Calender line tension of 1.8–2.3 kN/m is maintained to prevent ply puckering.

    End-use items. M24-grade abrasion-resistant top covers, M-grade secondary covers for overland bauxite transport belts, and hot-material elevator bucket flanges operating up to 120 °C continuous.

    Low-density microcellular soles manufactured from NR/BR blends employing sulfur cure systems present a process safety conflict: the accelerator must supply sufficient scorch delay to fill a multi-cavity mold yet generate a rapid cure at expanded-states to prevent cell collapse. In a typical blown-outsole formulation using activated 4,4'-oxybis(benzenesulfonyl hydrazide) (OBSH) as a blowing agent, MDB is added at 1.0–1.5 phr with 2.0 phr sulfur and 2.5 phr zinc oxide. The Mooney scorch MS-t3 at 121 °C (ISO 289-1) extends to 14–18 min, allowing a 24-station carousel compression molder to cycle without premature vulcanization in the coldest cavities. The cured sole must pass the SATRA TM144:2023 whole-sole flex test for 100,000 cycles without visible crack initiation, and the ISO 20871:2018 (DIN abrader) specific wear rate must stay under 120 mm³. Regulatory conformity follows the REACH SVHC Candidate List for any restricted phthalates, Annex XVII for BPA migration, and the Azo-dye restriction (EU) 2023/1110 for any pigmented systems. Terminal articles include injection-blown athletic technical shoes, vulcanized rubber workboot soles, and slip-resistant uniform footwear outsoles produced under ISO 20347:2021 certification.

    When dynamic engine mount compounding calls for zero-failure heat aging beneath aluminum brackets

    Automotive engine mounts and subframe bushings molded from NR/SBR blends must survive a continuous thermal soak of 150 °C for 504 hours while retaining at least 60% of their original dynamic shear modulus (G*) at 100 Hz. MDB, incorporated at 0.8–1.5 phr with a low-sulfur (0.8 phr) / high-accelerator (semi-EV) cure system, yields a tight monosulfidic and disulfidic crosslink distribution that limits the thermo-oxidative chain scission responsible for the fall in spring rate. When the cured compound is subjected to the cyclic compression test of ISO 2240-2:2022 for 1 million cycles, the set is maintained below 10%. Importantly, operators must be aware that residual morpholine outgassing at service temperatures above 120 °C can corrode the AlSi10Mn alloy bodies of lightweighted bracket castings; a post-cure baking step of 4 hours at 100 °C in a forced-ventilation oven is prescribed to strip volatile decomposition products.

    Conformance checklist. ASTM D2000-18 M4BG 714 designation, VDA 675-105 (elastomeric bushings dynamic stiffness, method A), and GME 00263 for hot creep under constant load.

    Manufacturing line. The compound is strip-fed into a 300-tonne injection molding press (Krupp Elastomertechnik DESMA 3200) with a cold-runner system run at 50 °C. Injection pressure is 80–110 MPa and cure time 180 seconds at 175 °C; cavities are degassed twice in the first 15 seconds to eliminate trapped air around the aluminum insert.

    Assembled products. Hydro-elastic engine mounting bodies, pendulum-style torque rods, twist-beam axle bushings, and cab-suspension bobbins for medium commercial trucks.

    Coolant Hose Tube Compounds and Extractable Amine Limits in Closed-Loop Coolant Systems

    The inner tube of an EPDM-based automotive radiator hose must withstand long-term contact with a 50:50 glycol/water mixture at 125 °C and 2.2 bar overpressure while maintaining a total extractables level below 15 mg/g after 96 h boiling ASTM D471-22 immersion. In this curing system, MDB is restricted to a narrow window of 0.5–0.8 phr with 1.0 phr of a thiuram polysulfide co-accelerator and 0.5 phr of an ultra-accelerator to complete the network while minimizing free morpholine extractables. The vulcanizate must exhibit a volume swell not exceeding 10% (IRM 903 oil reference), a burst pressure above 1.2 MPa (ISO 3862-2:2023), and zero crack after an ozone exposure of 200 pphm for 72 h at 20% elongation (ISO 1431-1:2022).

    Enforced specifications. SAE J20 Type EC classification for ethylene-propylene coolant hoses, ASTM D380-21 dimensional tolerances, and GM 6258M for extraction-stain resistance on aluminum cooling-system components. Additionally, sub-component chemical emission restrictions of GB 24409-2020 (China VI) apply to outlet markets requiring zero-N-nitrosamine testing.

    Process integration. Tubing is extruded on a 60 mm cold-feed vented extruder (L/D=14) with a crosshead die directly onto a woven aramid or polyester braid, followed by a cover layer. The uncured composite is placed on a mandrel and cured in an autoclave with saturated steam at 160 °C for 30 minutes. Post-cure devolatilization for 2 h at 130 °C strips residual morpholine, ensuring compliance with the VOC measurement limit of 50 µgC/g under VDA 278:2023.

    Production hose types. Engine coolant upper and lower radiator hoses, heater core hoses, and turbocharger coolant feed lines operating in a -40 °C to +135 °C fluid range.

    Table 1. Typical MDB Loading Ranges and Mooney Scorch Sensitivity in Key Elastomer Matrices
    Elastomer SystemMDB Loading (phr)Co-Accelerator (phr)Mooney Scorch MS-t5 at 120 °C (min)aRheometer t90 at 160 °C (min)b
    NR (SMR CV60)0.8–1.222–358.0–11.0
    SBR 1502 / BR 9000 (70/30)1.0–1.5DPG 0.225–406.5–9.0
    EPDM (4.8% ENB, low dicyclopentadiene)1.0–1.8TMTD 0.5 + ZDBC 0.218–303.5–6.0
    NR/BR (60/40 conveyor cover)0.6–1.2TMTM 0.316–265.5–8.0
    a Measured per ISO 289-1:2018 using large rotor; test temperature 120 °C. b Measured per ISO 6502-3:2018 at 160 °C, arc 0.5°, 60 min acquisition. Ranges represent typical production lot excursions documented across 12-month compound monitoring programs; absolute values shift with carbon black grade and oil dilution.
    Table 2. Compliance Standard Matrix per Application Scenario
    ScenarioSafety / EmissionPhysical TestVendor-Specific Specification
    Tire TreadREACH Annex XVII PAH, (EU) 2020/740ISO 4662 (rebound), UN R117 (RR)ETRTO 20.11
    Steel Cord BeltGHS Rev.9 (OEL morpholine)ASTM D2229, ISO 5603Michelin DMO 1092
    EPDM Weatherstrip Sponge93/11/EEC N-nitrosamine, EN 12868DIN 75201-B, VDA 270GMW15815, VW TL 52053
    Conveyor Belt CoverMSHA CFR 30 Part 18ISO 4649, ISO 10247AS 1332
    Footwear SoleAnnex XVII BPA, (EU) 2023/1110 azoSATRA TM144, ISO 20871ISO 20347
    Engine MountNone (VOC post-cure)ISO 2240-2, ISO 815-1GME 00263, VDA 675-105
    Coolant Hose TubeVDA 278, GB 24409ASTM D471, ISO 3862-2SAE J20 EC, GM 6258M
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    Certification & Compliance
    More Introduction
    2-(4'-Morpholinodithio)benzothiazole belongs to the sulfenamide–disulfide class of delayed-action accelerators, in which a benzothiazole ring is linked to a morpholinothio fragment through a disulfide bond. The molecular architecture imparts a distinct balance of processing safety and cure rate, placing the compound between conventional thiazoles and the faster-acting sulfenamides. Typical product models carry designations such as MDB and MOR-90 in industrial supply chains, with physical forms including a light-yellow to off-white powder or microgranules. Specifications accepted in vulcanization-grade shipments list an assay not less than 96.0% (by iodometric titration), a melting range of 130–136 °C (capillary method, heating rate 1 °C·min⁻¹), loss on drying below 0.5% (ISO 787-2, 2 h at 105 °C), and sulphated ash content limited to 0.3% (ISO 787-8). Bulk density, typically 0.55–0.70 g·cm⁻³, is supplied for silo dimensioning in automated feeding systems.

    Why Does 2-(4'-Morpholinodithio)benzothiazole Outperform Standard Thiazoles in High-Temperature Curing?

    The performance edge over benzothiazyl disulfide (MBTS) and 2-mercaptobenzothiazole (MBT) originates in the homolytic cleavage of the disulfide bridge at temperatures above 140 °C. Non-isothermal differential scanning calorimetry (DSC) according to ASTM E2041 at a heating rate of 10 °C·min⁻¹ reveals an exothermic onset at 168 ± 2 °C, which corresponds to the decomposition of the morpholinodithio group. The apparent activation energy derived by the Kissinger method is 85 ± 3 kJ·mol⁻¹, significantly lower than that of MBTS, enabling a well-defined critical temperature for accelerator fragmentation. The cleavage releases 2-mercaptobenzothiazole and a morpholinylthiyl radical; the latter abstracts a labile hydrogen from the polymer chain or a co-agent, generating active accelerator species while the 2-mercaptobenzothiazole moiety interacts with zinc oxide and stearic acid to form a zinc–sulphur complex. This stepwise activation mechanism produces a pronounced scorch delay—Marked as t₅ in Mooney scorch testing (ASTM D1646, large rotor, 121 °C)—that extends beyond that of CBS by 35–55% in a standard ASTM natural-rubber tread recipe (NR 100, N330 carbon black 50, zinc oxide 5.0, stearic acid 2.0, sulphur 2.25 phr). Under identical loading of 0.6 phr, t₅ values of 28–34 min are consistently recorded on-site with a 200 mm two-roll mill running at a friction ratio 1:1.2 and a measured stock temperature of 60–70 °C, whereas analogous CBS-stabilized batches give scorch times of 18–24 min. The widened window does not compromise cure rate: moving-die rheometer data (MDR, ASTM D5289, 150 °C, arc 0.5°) show a t₉₀ between 5.2 and 6.0 min, keeping cycle times commercial. When semi-efficient vulcanization systems demand high reversion resistance, the morpholine fragment introduces a secondary benefit. Thermogravimetric analysis under nitrogen (ISO 11358-1, 20 °C·min⁻¹) demonstrates that the residual mass after isothermal curing at 160 °C decays 12–15% less rapidly than in MBTS-cured analogues, a metric correlated with retained crosslink density measured by equilibrium swelling according to Flory–Rehner (ASTM D6814). This behaviour is exploited in truck-tire tread compounds where service temperatures routinely exceed 100 °C.

    Chemical and Physical Specifications

    Lot-release criteria for MDB technical grade
    ParameterSpecificationTest Method
    AppearanceLight yellow to off-white powder or microgranulesVisual, supplemental microscopy at 50×
    Assay (as C₁₁H₁₂N₂OS₃)96.0%Iodometric titration after acid hydrolysis
    Melting range130–136 °CCapillary, heating rate 1 °C·min⁻¹
    Loss on drying0.5%ISO 787-2 (105 °C, 2 h)
    Sulphated ash0.3%ISO 787-8
    Bulk density0.55–0.70 g·cm⁻³Graduated cylinder, tapped 100 times
    Residue on 100 μm sieve0.1%ISO 787-7
    Solubility in toluene (5% w/v, 25 °C)Clear solutionVisual, filter through 0.5 μm membrane
    Scorch Safety During High-Shear Mixing In a commercial installation equipped with an intermeshing internal mixer (chamber volume 160 L, fill factor 0.75, ram pressure 0.5 MPa, rotor speed 40 rpm), 2-(4'-morpholinodithio)benzothiazole is added in the mastication phase together with zinc oxide and stearic acid. The peak power draw during the first 30 s of dispersion rises to 18.5 ± 1.2 A (motor 600 V) and decays to 13.0 A within 2 min, the drop reflecting plastication of the NR phase and effective wetting of the accelerator powder. Mooney viscosity (ML1+4, 100 °C), measured on samples discharged at a dump temperature of 115–120 °C, stabilises at 52–56 MU versus 65–70 MU for an identically processed MBTS-based batch. The lower compound viscosity directly translates into a 15–20% reduction in extrusion head pressure observed on a 90 mm cold-feed pin-barrel extruder (L/D 16:1, screw speed 25 rpm, die swell 28–32%). Rapid plasticity gain, however, does not compromise green strength; tensile testing of uncured strips according to a modified ASTM D412 shows a yield stress of 2.8 MPa at 450% elongation, sufficient for bias-ply carcass building operations. Pre-drying is essential when ambient relative humidity exceeds 60%, because moisture uptake above 0.4 wt% causes agglomeration in loss-in-weight feeders, and trace water catalyses premature disulfide exchange that can reduce the scorch delay by 8–12% as recorded by a 1-min drop in t₅ in laboratory-controlled humidity trials.

    Mooney Scorch and Vulcameter Data: MDB Versus Competing Accelerator Systems

    The following comparison incorporates a fixed filler–polymer matrix (NR/SBR 60/40, silica 35 phr, carbon black N234 15 phr, silane coupling agent Si69 2.8 phr) to isolate the accelerator’s contribution. All figures are means of five independent replicates obtained from a single lot.
    Comparative rheometric and physical properties at 0.8 phr accelerator loading
    AcceleratorMooney scorch t₅ (121 °C, min) ASTM D1646MDR t₉₀ (150 °C, min) ASTM D5289MH−ML (dNm)Tensile strength (MPa) ASTM D412Elongation at break (%)
    MDB30.2 ± 1.15.8 ± 0.215.322.4460
    CBS21.5 ± 0.94.2 ± 0.214.821.9445
    MBTS12.3 ± 0.73.9 ± 0.115.920.1415
    TBBS (N-tert-butylbenzothiazole-2-sulfenamide)24.6 ± 1.34.1 ± 0.215.523.0450
    The data underscore the longer processing window of MDB without sacrificing the rate of vulcanization beyond what an ISO 9001-controlled mixing line can tolerate. The torque increment (MH−ML) remains statistically equivalent to that of TBBS and CBS, indicating that the final crosslink density is not diluted by the morpholine fragment. Tear resistance measured by Grabia’s method (ASTM D624, die C) also shows a small but reproducible improvement of 8–10% over CBS, attributed to a more homogeneous network structure evidenced by lower residual free sulphur content (detected by liquid chromatography after 24 h reflux in acetone). When FDA 21 CFR 177.2600 Governs Accelerator Selection Regulatory acceptance for rubber articles intended for repeated use in contact with food draws on the status of 2-(4'-morpholinodithio)benzothiazole as a derivative of benzothiazyl disulfide, an approved substance under 21 CFR 177.2600(c)(3). Migration limits specified in the same regulation—0.5 mg per square inch of food-contact surface—are met when the compound is cured at a temperature above 150 °C and followed by a post-cure water boil of 2 h, as confirmed by extraction testing with n-heptane according to ASTM F1306. For applications that fall under EU Regulation (EC) No 1935/2004, the finished article must additionally satisfy overall migration limits of 10 mg·dm⁻² specified by Commission Regulation (EU) No 10/2011, though the substance is not listed explicitly in the Union positive list; therefore, a case-by-case conformity assessment is required, typically supported by worst-case migration calculations performed at 40 °C for 10 days in 3% acetic acid. In all such regulated environments, accidental combination with amine-based ultra-accelerators (e.g., di-o-tolylguanidine) must be avoided, because alkalinity from the amine raises the pH of the rubber matrix above 9.5, which accelerates disulfide bond solvolysis and can reduce the scorch safe time by more than 60% in internal mixer trials, essentially collapsing the process window. Storage stability under REACH registration (EC) 1907/2006 is documented at 25 °C in sealed, nitrogen-flushed 25 kg HDPE bags; when these conditions are maintained, the active content drops by less than 0.2% over 12 months, confirmed by lot re-analysis.