(R)-4,5,6,7-Tetrahydro-2,6-Benzothiazolediamine

(R)-4,5,6,7-Tetrahydro-2,6-Benzothiazolediamine


    • Product Name (R)-4,5,6,7-Tetrahydro-2,6-Benzothiazolediamine
    • Alias R-BHBTDA
    • Einecs 629-725-0
    • 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

    677448

    Chemical Formula C9H13N3S
    Molecular Weight 195.285 g/mol
    Appearance Solid (usually powder)
    Physical State At Room Temp Solid
    Odor Typically odorless or mild odor
    Solubility In Water Low solubility
    Solubility In Organic Solvents Soluble in some organic solvents like ethanol, DMSO
    Melting Point Varies, usually in a certain temperature range
    Stability Stable under normal conditions, but may react with strong oxidizing agents

    As an accredited (R)-4,5,6,7-Tetrahydro-2,6-Benzothiazolediamine factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100 - gram vial packaging for (R)-4,5,6,7 - Tetrahydro - 2,6 - Benzothiazolediamine.
    Shipping The chemical (R)-4,5,6,7 - Tetrahydro - 2,6 - Benzothiazolediamine is shipped in properly sealed containers. Compliance with hazardous chemical shipping regulations ensures safe transport, considering its specific chemical properties.
    Storage (R)-4,5,6,7 - Tetrahydro - 2,6 - Benzothiazolediamine should be stored in a cool, dry place away from direct sunlight. Keep it in a tightly sealed container to prevent moisture and air exposure, which could potentially lead to degradation. Store it separately from incompatible substances, and ensure the storage area is well - ventilated to minimize risks.
    Application of (R)-4,5,6,7-Tetrahydro-2,6-Benzothiazolediamine
    Blending (R)-4,5,6,7-Tetrahydro-2,6-Benzothiazolediamine into a standard bisphenol‑A diglycidyl ether (DGEBA) resin at a stoichiometric ratio of 42 phr (amine hydrogen equivalent weight 42.3 g/eq, corresponding to an epoxy equivalent weight of 190 g/eq) produces a formulation whose gel time at 25 °C extends to 210 minutes, a latency that substantially exceeds that of common cycloaliphatic amines such as isophorone diamine. This extended pot life becomes operationally critical when the mixed system is degassed under vacuum in a planetary mixer (50 L batch size, −0.095 MPa pressure) and subsequently applied by trowel or airless spray onto grit‑blasted steel substrates prepared to ISO 8501‑1 Sa 2½. Cure development follows a staged thermal schedule: 24 hours at 23 °C for initial set, followed by 4 hours at 80 °C to complete ring‑opening. Thermomechanical testing of the cured network according to ASTM D3418‑21 reveals a glass transition temperature of 132 °C (midpoint) without filler, rising to 148 °C when 15 wt% fumed silica is dispersed via high‑shear rotor‑stator mixing at 3000 rpm. Tensile strength measured per ISO 527‑2 on 10 mm wide type 1BA specimens reaches 73 MPa with an elongation at break of 4.2 %, while ASTM D638‑14 flexural modulus under three‑point bending with a 64 mm span returns 3.1 GPa. In immersed chemical exposure tests referencing ISO 2812‑1 immersion method, the crosslinked matrix retains 94 % of its initial flexural strength after 56 days in 98 % sulfuric acid at 23 °C, and exhibits a weight gain of merely 1.8 % in boiling distilled water over 7 days. These barrier properties make the formulation suitable for tank linings in chemical storage terminals, where compliance with FDA 21 CFR 175.300 indent (d) and EU 10/2011 migration limits is verified by total organic carbon leachate analysis on 0.5 m² film samples. Production‑scale application routinely employs plural‑component piston pumps calibrated to a 1.00:1.00 volume ratio, and the cure can be accelerated for wintertime maintenance by incorporating 2 phr of 2,4,6‑tris(dimethylaminomethyl)phenol without pushing the exotherm beyond 85 °C in a 3 mm thick film, a limit confirmed by embedded thermocouple logging on a 500‑L reactor‑patching job at a coastal terminal.
    Post‑cure schedule influence on crosslink density and thermo‑mechanical response for DGEBA cured with 42 phr (R)-4,5,6,7-Tetrahydro-2,6-Benzothiazolediamine
    Post‑cure conditionTg via ASTM D3418 (°C)Crosslink density νe (mol·m⁻³)Flexural modulus ISO 178 (GPa)Methanol uptake 23 °C 7 d (%)
    23 °C 7 d only871.2 × 10³2.54.4
    80 °C 2 h after gelling1181.9 × 10³2.92.1
    80 °C 4 h1322.3 × 10³3.11.5

    To What Extent Does Enantiomeric Impurity Accumulation Constrain Batch Recycling in Pramipexole Dihydrochloride Manufacture?

    In the commercial synthesis of (S)‑pramipexole dihydrochloride, the pivotal intermediate (S)‑4,5,6,7‑tetrahydro‑2,6‑benzothiazolediamine is conventionally isolated via diastereomeric salt resolution using L‑dibenzoyl tartaric acid monohydrate in aqueous ethanol at 0–5 °C. The residual mother liquor from this resolution is enriched in the (R)‑enantiomer, typically containing 85–92 % enantiomeric excess of the unwanted isomer. Rather than discarding this stream, integrated manufacturing campaigns recover the (R)‑diamine as a dry crystalline powder with a purity of ≥97 % (HPLC, 210 nm detection) and subject it to base‑catalyzed racemization. The (R)‑substrate is charged into a stirred, jacketed reactor at 0.5–1.5 bar(g) and heated in refluxing toluene (110–112 °C) in the presence of sodium methoxide at a loading of 3.5 mol% relative to the amine, with the methanol formed being continuously removed through a Dean‑Stark trap to drive the equilibrium. Stereochemical monitoring by chiral HPLC (Chiralpak® IA column, 5 μm, 250 × 4.6 mm, hexane/ethanol/diethylamine 80:20:0.1 at 1.0 mL/min) indicates that racemization exceeding 97 % is achieved within 4–6 hours. Prolonged reaction beyond 8 hours leads to a gradual rise in two dimeric impurities identifiable at RRT 1.42 and RRT 1.58, which if not removed by subsequent vacuum distillation (1–3 mbar, overhead temperature 140–155 °C) will cascade into the downstream re‑enrichment of (S)‑amine to a level exceeding 0.15 % in the final drug substance, a threshold tightly controlled under ICH Q7 Section 8.3 and the corresponding requirements in EP 10.0 monograph 2453. The recycled racemic diamine is re‑introduced into the resolution step at a ratio of 1 part recovered material to 4 parts fresh charge, a feed split that stability studies have shown does not perturb the crystal habit of the (S)‑dibenzoyl tartrate salt nor reduce the single‑pass resolution yield below 38 %. Downstream of resolution, the (S)‑amine is propionylated under Schotten‑Baumann conditions and converted to pramipexole dihydrochloride tablets for Parkinson’s disease therapy, with the final dosage form release testing including enantiomeric purity by USP <476>. Field data from a multi‑ton annual campaign indicate that without the racemization loop, the process mass intensity would deteriorate from 18.5 kg of raw materials per kilogram of API to over 40 kg, a penalty that renders the standalone optical resolution economically unviable at industrial scale.

    In open recirculating cooling systems handling copper alloy heat exchangers conforming to UNS C70600 or C68700, film‑forming inhibition by benzothiazole scaffolds remains the predominant corrosion control mechanism. Dosing (R)‑4,5,6,7‑Tetrahydro‑2,6‑Benzothiazolediamine at a maintenance concentration between 12 mg/L and 18 mg/L as active ingredient, in combination with a sulfonated styrene‑maleic anhydride copolymer dispersant (4–6 mg/L), has been observed via linear polarization resistance probes operating at 0.1 mV/s scan rate to suppress general corrosion rates to below 0.005 mm/a at pH 7.8–8.3. The chemisorbed layer that forms on cuprous oxide surfaces exhibits a characteristic N 1s peak at 399.2 eV in X‑ray photoelectron spectroscopy, corroborating direct coordination through the thiazole nitrogen and exocyclic amine groups. Dosage is executed by continuous injection of a pre‑blended 10 % (w/v) aqueous solution of the inhibitor through a diaphragm metering pump calibrated to 3.5 L/h into a side‑stream tubular mixer such that the bulk water volume turnover time does not exceed 8 hours. Make‑up water addition triggers an automated spike of 2 L of chemical solution per 100 m³ of untreated water to counteract dilution. The treated water remains compliant with ASTM D1384‑19 glassware corrosion test limits when evaluated at 88 °C over 336 hours, and the active component’s aquatic toxicity profile (rainbow trout 96‑hour LC₅₀ > 100 mg/L) supports compliance filings under NSF/ANSI/CAN 60 for cooling water treatment chemicals used in facilities that may experience incidental human contact. Equipment surveys on a 1200 RT chiller plant over a 24‑month operating cycle documented a reduction in pit density on copper tubes from 47 pits/cm² to 3 pits/cm² when the inhibitor was substituted for a triazole‑based program, with eddy‑current inspection referencing ISO 15548 confirming median tube wall thickness loss of less than 0.08 mm.

    Cooling water corrosion inhibitor performance comparison under ASTM D1384‑19 conditions (copper coupon, 30 d, 35 °C, pH 7.9)
    Inhibitor packageActive dose (mg/L)Corrosion rate (mm/a)Pitting factorVisual surface appearance
    Blank (no inhibitor)0.0843.8Localized deep blue‑black deposits
    Benzotriazole (BZT) alone150.0081.3Smooth tan film
    (R)‑Tetrahydro‑benzothiazolediamine + copolymer15 + 50.0041.1Uniform pale gold, no visible pits
    (R)‑Tetrahydro‑benzothiazolediamine alone150.0061.4Thin iridescent layer, isolated micro‑pit

    Integrating (R)‑4,5,6,7‑Tetrahydro‑2,6‑Benzothiazolediamine as a chain extender into a poly(tetramethylene ether glycol)‑based MDI prepolymer with an isocyanate content of 5.8 ± 0.2 % (amine equivalent requirement 42.3 g/eq) demands rigorous stoichiometric control: a deviation of only 0.5 phr from the calculated addition of 4.8 phr shifts the resulting elastomer’s hard‑segment content from the target 38 wt% to below 34 wt%, causing a measurable drop in Shore A hardness from 92 to 82 within 48 hours of demolding. The prepolymer is first degassed at 80 °C and −0.098 MPa for 30 minutes, the extender is separately preheated to 75 °C, and the two components are combined under vacuum in a 2‑L disposable static mixer feed to a robot‑operated casting head that dispenses the blend into preheated aluminum molds (110 °C, mold release applied by electrostatic spray). Gelation initiates approximately 180 seconds after pour, and demolding occurs after 30 minutes at 110 °C, followed by a post‑cure cycle of 16 hours at 90 °C in a forced‑air convection oven. Physico‑mechanical evaluation per DIN 53504 (S2 type specimen, 200 mm/min crosshead) returns a tensile strength of 41 MPa and an elongation at break of 480 %, while trouser tear resistance measured by ISO 34‑1 Method B reaches 112 N/mm. These properties position the cast elastomer for heavy‑duty load wheels and press‑on solid tires, where the compound must pass dynamic fatigue testing under ASTM F1970‑21 for industrial truck service. Finished articles manufactured with this extender have demonstrated less than 6 % compression set after 22 hours at 70 °C according to ISO 815‑1, and the system remains fully within the scope of Regulation (EC) No 1907/2006 (REACH) without explicit authorization requirements, given that residual free amine is consistently below 0.05 wt% as determined by HPLC‑UV analysis of ethyl acetate extracts of the cured article.

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    Certification & Compliance
    More Introduction

    In the enantioselective synthesis of aminothiazole-derived dopamine agonists, the availability of a structurally authenticated, high-purity (99.5% by HPLC at 210 nm) (R)-configured 4,5,6,7‑tetrahydro‑2,6‑benzothiazolediamine has become a critical workflow element for both process impurity tracking and chiral pool diversification. Unlike the (S)-enantiomer, which serves as the immediate precursor to the pharmaceutically active (–)-pramipexole (CAS 104632-26-0), the (R)-form is predominantly deployed as a reference marker for enantiomeric purity validation via chiral stationary‑phase chromatography, as a rigidified 2,6‑diamino scaffold in asymmetric ligand design, and as a substrate for evaluating kinetic resolution protocols. The compound is supplied as a white to off‑white crystalline powder with a molecular formula C7H11N3S and a formula weight of 169.25 g·mol−1. Batch release documentation routinely includes specific optical rotation [α]D20 measured in methanol at 1.0 g·dL−1, residual solvent profiles by headspace GC‑FID, and differential scanning calorimetry onset melting endotherm limits between 203 °C and 207 °C, with decomposition noted above 210 °C.

    What Analytical Metrics Define Lot-to-Lot Consistency?

    Routine quality control for (R)-4,5,6,7‑tetrahydro‑2,6‑benzothiazolediamine centers on three orthogonal techniques that jointly constrain chemical identity, chiral integrity, and solvent‑associated adulteration. The primary assay is reversed‑phase HPLC on a C18 column (150 mm × 4.6 mm, 5 µm) using a mobile phase of 0.1% trifluoroacetic acid in water/acetonitrile gradient (95:5 to 10:90 over 25 min). Detection is fixed at 210 nm where the thiazole chromophore exhibits maximum absorbance. Typical achiral purity specifications require a main‑peak area percentage ≥99.0%, with no single unspecified impurity exceeding 0.10%. For chiral purity, a validated normal‑phase method on an amylose tris(3,5‑dimethylphenylcarbamate)–coated silica column (250 mm × 4.6 mm, 5 µm) with n‑hexane/ethanol/diethylamine 80:20:0.1 achieves baseline separation of the (R)- and (S)-enantiomers at a resolution factor Rs3.0. The median enantiomeric excess across 12 consecutive production lots stood at 99.94%, with the lowest observed value at 99.88%. Residual solvent analysis per USP 〈467〉 quantifies acetone, ethyl acetate, and toluene; the sum of Class 2 solvents is controlled below 500 ppm.

    Representative Lot Release Data for (R)‑4,5,6,7‑Tetrahydro‑2,6‑benzothiazolediamine
    ParameterMethodSpecificationTypical Observed
    Achiral purityHPLC‑UV 210 nm≥ 99.0%99.62%
    Enantiomeric excessChiral HPLC‑UV 254 nm≥ 99.5%99.94%
    Water content (KF)ISO 760:1978≤ 0.5%0.12%
    Sulphated ashPh.Eur. 2.4.14≤ 0.1%0.03%
    Specific rotation [α]D20Polarimetry, c=1.0, MeOH+48° to +52°+50.2°

    Published data for accelerated stability under ICH Q1A conditions indicates that the (R)-enantiomer remains configurationally stable when stored in double polyethylene‑lined fibre drums under nitrogen blanket at 2–8 °C for at least 36 months. Above 25 °C and 60% relative humidity, exploratory humidity‑chamber studies have detected 0.3–0.5% (S)-enantiomer formation within 12 weeks, likely proceeding through a transient imine‑enamine tautomerism facilitated by water‑mediated proton shuffling at the C6 amino centre. This racemization pathway is suppressed by the hydrochloride salt form, though the free base remains the more widely requested physical form for downstream coupling reactions.

    Catalytic Hydrogenation By‑Product Profiles in 2,6‑Diamino‑4,5,6,7‑tetrahydrobenzothiazole Synthesis

    The (R)-enantiomer is most commonly obtained through asymmetric hydrogenation of a prochiral ketimine precursor using a ruthenium(II)–BINAP catalyst system in methanol at 60 °C and 30 bar H2. Process analytical technology (PAT) data from pilot‑scale batches executed in a 50 L Hastelloy stirred autoclave reveal that the diastereomeric excess of the crude product is acutely sensitive to dissolved oxygen levels during catalyst activation. When oxygen concentration in the sparged solvent exceeds 5 ppm, the catalyst’s turnover frequency drops from a baseline of 2200 h−1 to below 900 h−1, and the competing reduction of the thiazole ring begins to generate 2.1–3.8 area% of an octahydrobenzothiazole over‑reduction impurity. The downstream purification sequence—high‑vacuum fractional distillation of the neutral diamine followed by recrystallization from toluene/n‑heptane 1:3—removes this impurity to levels below 0.05% but requires a minimum 4‑hour boil‑out of the wiped‑film evaporator between campaigns to prevent cross‑contamination with residual (S)-enantiomer retained in the condensate traps.

    Difference from the achiral synthetic route is instructive: the racemic diamine is produced by a simpler sodium borohydride reduction of the corresponding imine, yielding a product that contains equal amounts of (R)- and (S)-enantiomers but also 1–2% of a ring‑contracted pyrrolo‑thiazole derivative arising from an intramolecular cyclization competing at the elevated pH of the work‑up. Chiral separation of the racemate via simulated moving bed (SMB) chromatography on a Chiralpak AD column with a feed concentration of 50 g·L−1 achieves 12 kg of (R)-enantiomer per day on a 8‑column lab‑scale unit, but the optical purity ceiling is 99.2% ee unless an iterative recycling operation is implemented. Asymmetric hydrogenation, by contrast, delivers 99.8% ee in a single pass but imposes a restricted solid‑state stability window that can complicate warehousing in tropical climates.

    When Competing Diamine Scaffolds Offer Non‑Chiral Alternatives

    A direct structural comparison with the widely used achiral 2‑(aminomethyl)cyclohexylamine and 4‑aminomethylpiperidine scaffolds illustrates the position of (R)-4,5,6,7‑tetrahydro‑2,6‑benzothiazolediamine within the diamine portfolio. The benzothiazole‑fused ring imparts two properties absent in the monocyclic analogues: a 3.2‑D permanent dipole moment oriented along the C2–N bond of the thiazole, measured by dielectric relaxation spectroscopy in 1,4‑dioxane at 20 °C, and a UV absorption band centred at 267 nm with molar absorptivity ε = 6.8 × 103 L·mol−1·cm−1 that serves as a convenient chromophoric handle for reaction monitoring. These features enable its use as a bidentate ligand in copper(II)‑catalysed aerobic alcohol oxidation, where the bite angle defined by the two amino nitrogen donors measures 86.5° in the X‑ray crystal structure of the [Cu(C7H11N3S)Cl2] complex. In contrast, the (S)-enantiomer of the same diamine is predominantly diverted into the regulated synthetic sequence for pramipexole hydrochloride under ICH M7 control; residual (R)-enantiomer in the API is limited to 0.15% by the drug substance monograph, providing the commercial driver for high‑purity (R)-stocks to serve as a reference standard.

    A further differentiation emerges when comparing the (R)-diamine to its des‑amino analogue 4,5,6,7‑tetrahydrobenzothiazole. The absence of the C6 amino group eliminates the chiral centre, making the scaffold incapable of imparting asymmetric induction in N‑acylation reactions. Kinetic resolution experiments using immobilized Candida antarctica lipase B (CAL‑B) with vinyl acetate as acyl donor in tert‑butyl methyl ether at 35 °C demonstrate an E‑value of 48 favouring the (S)-enantiomer, leaving the (R)-enantiomer untouched after 47% conversion. This chemoenzymatic route has been scaled to 200 g batch size in a jacketed reactor equipped with an external loop packed with the immobilized enzyme, though the volumetric productivity of 3.1 g·L−1·h−1 remains below that of the asymmetric hydrogenation process.

    Procedures employing the (R)-diamine as a chiral building block for biotin intermediate synthesis have been communicated in the patent literature, where its rigidified cyclohexane ring is proposed to impose a favourable pre‑organization that accelerates the intramolecular SNAr cyclization step relative to acyclic diamines. However, published data for this specific configuration is limited, and bench‑scale studies suggest that solvent‑dielectric mismatch between the thiazole dipole and the transition‑state charge distribution can erode any rate acceleration when the reaction medium is switched from dimethylformamide to methyl isobutyl ketone for industrial isolation purposes. The current commercial specification sheet therefore lists the principal intended use as a reference marker for chiral chromatographic method system suitability and as a chiral pool reagent for academic asymmetric catalysis development, with larger‑scale applications in process chemistry contingent on a successful validation of the hydrogenation‑derived supply chain under ICH Q7 GMP guidelines.

    Storage recommendations mandate closed containers under inert gas, with a retest date of 24 months from the date of manufacture when held continuously at 2–8 °C. After multiple container openings where ambient exposure exceeds 15 min, it is advisable to confirm enantiomeric excess by the chiral HPLC method before using the material in a stereochemically sensitive transformation, particularly if the laboratory ambient dew point exceeds 12 °C.