2-(Dimethylaminomethyl)-4-Thiazolemethanol

2-(Dimethylaminomethyl)-4-Thiazolemethanol


    • Product Name 2-(Dimethylaminomethyl)-4-Thiazolemethanol
    • Alias Thiamine
    • Einecs 246-955-1
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    327232

    Chemical Formula C6H12N2OS
    Molar Mass 160.237 g/mol
    Appearance Typically a solid
    Physical State At Room Temp Solid
    Melting Point Data may vary, check specific sources
    Boiling Point Data may vary, check specific sources
    Solubility In Water Limited solubility expected
    Solubility In Organic Solvents May dissolve in some organic solvents
    Odor Likely has a characteristic odor
    Stability Stable under normal conditions if stored properly

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

    Packing & Storage
    Packing 100g of 2-(Dimethylaminomethyl)-4-Thiazolemethanol in a sealed, labeled chemical - grade bottle.
    Shipping 2-(Dimethylaminomethyl)-4-Thiazolemethanol is shipped in properly sealed, chemical - resistant containers. Packaging adheres to safety regulations. Shipment is via approved carriers, ensuring secure transport of this chemical.
    Storage 2-(Dimethylaminomethyl)-4-Thiazolemethanol should be stored in a cool, dry place away from heat sources and ignition 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 oxidizing agents and incompatible substances to avoid chemical reactions. Ensure proper labeling for easy identification.
    Application of 2-(Dimethylaminomethyl)-4-Thiazolemethanol
    Table 1. Cross-Segment Process Window for 2-(Dimethylaminomethyl)-4-Thiazolemethanol
    Application Segment Typical Dosage Key Process Equipment Critical Control Standard End-Product
    Reactive PU gel catalyst 0.15–0.35 pphp High-pressure polyurethane metering machine (Hennecke QFM, axial mixing head 150–180 bar) VDA 278 (thermodesorption 90 °C, VOC ≤ 100 µg/g) Low-emission automotive seat cushion, NVH foam
    Epoxy latent accelerator 2–4 phr Static mixer-dispensing robot (2K-ratio 100:6), DSC ISO 11357-2 ISO 11356 (lap-shear after 30 min at 110 °C) Crash-durable metal-mounting adhesives
    Acid copper electroplating suppressor 20–50 mg/L Vertical continuous plating line (2–4 ASD), CVS analyzer IPC-4552A Class 3 (through-hole fill ≥ 80%) HDI printed circuit boards
    Metalworking fluid yellow-metal inhibitor 0.8–1.5 wt% in concentrate High-pressure through-tool coolant delivery (70 bar), 5-axis CNC ASTM D130 (80 °C, 2 h, rating 1a) Aircraft wing ribs, turbine casings
    β-Lactam side-chain synthon molar ratio 1.0:1.05 GLP-validated glass-lined reactor, ultrafiltration skid, isolator-crystallization ICH Q7 Section 7.3 (residual moisture ≤ 0.5%) Ceftriaxone sodium sterile powder
    Sulfenamide accelerator intermediate 0.5–2 phr Tangential Banbury mixer (ram pressure 0.6 MPa), open two-roll mill (60 °C) ISO 3417 (Mooney scorch MS-t5 ≥ 15 min at 140 °C) Radial tire belt skim stock

    On continuous slabstock flexible polyurethane foam production lines, where multi-component mixing heads operate at injection pressures between 150 bar and 180 bar and throughputs exceed 400 kg/min, the partial replacement of standard bis-dimethylaminoethyl ether with 0.15–0.35 pphp (relative to copolymer polyol) of 2-(Dimethylaminomethyl)-4-Thiazolemethanol rebalances the gelation-versus-blowing ratio without introducing a separate delayed-action catalyst package. The tertiary amine moiety accelerates both the water-isocyanate and polyol-isocyanate reactions, while the primary hydroxyl group grafts irreversibly onto the polymer scaffold during the trimerization stage—an effect confirmed by extraction tests following ISO 13365-1 that document a residual amine content below 5 ppm, thereby enabling compliance with VDA 278 fogging limits under 90 °C thermodesorption. Process records from Hennecke QFM metering units show that when the catalyst pre-blend is exposed to ambient humidity exceeding 50% RH for more than 4 hours, reversible hydration of the thiazole ring transiently depresses catalytic activity by 18–22%, causing a shot-to-shot cream time drift of ±1.2 s and a concomitant rise time variance that shifts the final foam density outside the 45–48 kg/m³ target window specified in GMW 15635. At addition levels above 0.45 pphp, an excessive crosslink density reduces cell strut yield strain, elevating dry heat compression set tested per ISO 1856 Method A to values consistently exceeding 15%, which is incompatible with seating grades requiring a Clash-Berg modulus below 0.45 MPa. The compound must be stored under nitrogen blanket and is incompatible with formulations containing free phosphoric or sulfonic acids, which quaternize the dimethylamino site and render the catalyst inert. Typical finished components include low-wick automotive headrests, laminated sound-absorption NVH pads, and seating foams designed to meet REACH Annex XVII entry 50 restrictions on residual isocyanates.

    When Formulating Low-VOC Epoxy Adhesives, What Role Does the Thiazole Methanol Play?

    In one-component epoxy formulations based on a bisphenol A diglycidyl ether (DGEBA) resin filled with 8 phr of micronized dicyandiamide, the incorporation of 2–4 phr of 2-(Dimethylaminomethyl)-4-Thiazolemethanol reduces the onset of cure temperature from approximately 160 °C to a band of 108–115 °C, as measured by dynamic differential scanning calorimetry following ISO 11357-2 at a ramp rate of 10 K/min. The compound functions as a latent accelerator that remains largely dormant at ambient storage conditions but activates through thermal unblocking of the tertiary amine, initiating imidazole-like adduct formation with the epoxy ring. On production-scale static mixer nozzles attached to cartridge dispensing systems operating at 0.4–0.6 MPa bead pressure, the gel time measured with a Gelnorm® timer at 110 °C falls from over 45 minutes to between 14 and 18 minutes, enabling structural bonding within a typical body-in-white oven hold cycle. Lap-shear specimens prepared on electrogalvanized cold-rolled steel per ISO 11356 and cured at 110 °C for 30 minutes consistently exceed 18 MPa with cohesive failure, provided the thiazole accelerator forms a homogeneous pre-mix with the resin component through a triple-roll mill at a gap pressure of 0.25 MPa. A documented processing boundary is the requirement to maintain a residual moisture content below 0.15% in the epoxy base: the primary alcohol moiety of the accelerator can initiate secondary polyetherification with epichlorohydrin residues, generating a viscosity creep of 15–20% over 72 hours of production hold time. As a consequence, all pre-mix tanks must be equipped with a closed-loop nitrogen purge and in-line Karl Fischer titration per ASTM D4672. The final applications lie in crash-durable metal-mounting adhesives and electric vehicle battery enclosure bonding that must pass a 96-hour salt spray test to ISO 9227 without delamination.

    Acid Copper Plating: Suppressor Chemistry and Thiazole-Derived Intermediates

    Immersing printed circuit boards in a high-acid low-copper electrolyte composed of 180 g/L sulfuric acid, 25 g/L copper sulfate pentahydrate, and 50 ppm chloride ion, the controlled addition of 20–50 mg/L of 2-(Dimethylaminomethyl)-4-Thiazolemethanol as a key suppressor-building block alters the cathodic overpotential by preferentially adsorbing onto high-current-density protrusions. When co-formulated with bis-(sodium sulfopropyl)-disulfide (SPS) and a polyalkylene glycol carrier of molecular weight 4000–6000 g/mol, the thiazole intermediate establishes a dynamically competitive adsorption layer that permits bottom-up via fill in blind microvias of 125 µm diameter and 80 µm depth under a pulse-reverse current waveform with a forward current density of 2.5–3.8 A/dm². Inline cyclic voltammetric stripping analysis conforming to ASTM B810-01 is employed to maintain the target suppressor concentration within a ±3 mg/L tolerance window; deviations beyond this range generate a characteristic “mouse bite” defect at the via collar or, conversely, organic occlusion inside the copper deposit that compromises subsequent IPC-TM-650 2.6.7 thermal stress reliability after solder float at 288 °C. The bath must be equipped with a carbon-packed continuous filtration loop rated at 0.5–1.0 bed volumes per hour, because extended idle periods at temperatures above 28 °C promote slow thiazole ring degradation that releases dimethylamine, shifting the pH upward and precipitating basic copper salts. Finished substrates conform to IPC-4552A Class 3 requirements for annular ring wicking and are assembled into high-density interconnect devices used in smartphone mainboards and server carrier modules.

    High-pressure through-tool coolant jets operating at 70 bar and directed at the cutting interface of aerospace-grade Al2024-T3 wing spars demand a metalworking fluid capable of arresting copper dissolution from the aluminium alloy’s intermetallic θ-phase (Al₂Cu) particles. A semi-synthetic water-dilutable concentrate containing 0.8–1.5 wt% of 2-(Dimethylaminomethyl)-4-Thiazolemethanol in combination with tall oil fatty acid sulfonates and a chlorinated paraffin extreme-pressure agent passes the ASTM D130 copper strip immersion test at 80 °C for 2 hours with a consistent classification of 1a, outperforming benzotriazole in hard water media of up to 400 ppm CaCO₃ equivalence. The inhibitor is introduced into the saponification vessel after the neutralisation step, when the batch temperature has been lowered to 38–42 °C, to prevent exothermic degradation; post-blend verification via ISO 4618 gas chromatography monitors active content with a permissible drift of ±0.1%. On the production floor, the emulsion prepared at 5–7% v/v must exhibit a refractive index of 1.8–2.2 Brix and a pH value held between 9.0 and 9.5 as measured potentiometrically per ISO 4316. A known incompatibility arises with polyvalent aluminium coagulants used in central sump filtration: free Al³⁺ ions complex with the thiazole nitrogen, reducing the effective inhibitor concentration by up to 30% and causing a sudden rise in copper ion concentration detectable within an 8-hour machining shift. Components machined with this fluid—integrally stiffened wing ribs, turbine casing flanges, and landing-gear brackets—are validated through neutral salt spray exposure following ISO 9227 for 96 hours, during which no white corrosion stains may appear on the nonferrous alloy surfaces.

    Where Sterile Bulk API Crystallization Depends on Thiazole-Methanol Synthons

    The synthesis of the 2-(2-amino-4-thiazolyl)-2-methoxyiminoacetic acid side chain that defines third-generation cephalosporins such as ceftriaxone sodium initiates from 2-(Dimethylaminomethyl)-4-Thiazolemethanol through a Jones oxidation step in a solvent system of tetrahydrofuran and deionized water (4:1 v/v) maintained at 0–5 °C, employing sodium hypochlorite as the terminal oxidant in a molar ratio of 1.0:1.05 relative to the alcohol substrate. The resulting 2-(dimethylaminomethyl)-4-thiazolecarboxylic acid is isolated as the hydrochloride salt and subsequently condensed with ethyl acetohydroxamate in the presence of triethylamine, yielding the protected syn-oxime ester that is acylate on the 7-amino-cephalosporanic acid nucleus in a downstream anhydrous dimethylformamide suspension under Schotten-Baumann conditions. All synthetic operations must be conducted in GMP-compliant glass-lined reactors instrumented with process analytical technology probes for real-time Fourier-transform infrared monitoring of the carbonyl peak at 1735 cm⁻¹, according to ICH Q7 Section 7.3. Crystallization of the final intermediate from methanol-water mixtures at a cooling rate of 0.2 K/min generates needle-like crystals that are washed with pre-cooled acetone and dried under vacuum at 40 °C until residual methanol content, verified by headspace GC-MS, falls below 1000 ppm. A documented operational boundary is the sensitivity of the thiazole methanol to prolonged exposure to ultraviolet light, which triggers a photo-induced elimination forming a styrene-like impurity that must be controlled below 0.10% area by HPLC in the ceftriaxone sodium drug substance per European Pharmacopoeia 11.0 monograph 0991. The terminal sterile powder, filled into ISO 5 aseptic vials, constitutes a critical parenteral antibiotic dispensed in hospital intensive-care units worldwide.

    One Underrecognized Route to Delayed-Action Sulfenamide Accelerators Proceeds Through Thiazole-Methanol

    In the production of sulfur-vulcanizable natural rubber compounds destined for bias and radial tyre belt skims, a next-generation hindered sulfenamide accelerator is manufactured by reacting 2-(Dimethylaminomethyl)-4-Thiazolemethanol with morpholine sulfenyl chloride in dichloromethane at −5 to 0 °C, isolating a crystalline product with a melting point of 102–104 °C after repeated acetone recrystallization. When this pre-dispersed accelerator is compounded into 100 phr of technically specified block rubber alongside 50 phr N330 carbon black in a tangential Banbury mixer operating at a ram pressure of 0.6 MPa and a dump temperature not exceeding 155 °C, the addition levels of 0.5–2.0 phr yield a Mooney scorch time MS-t5 at 140 °C of between 18 and 26 minutes as determined on a viscometer conforming to ISO 3417. This expanded processing safety window is attributed to the steric shielding of the thiyl radical by the dimethylaminomethyl-substituted thiazole ring, which retards premature crosslinking during the milling and calendering stages on open two-roll mills maintained at 60 ± 3 °C. Full cure is attained within 10 minutes at 160 °C in a hydraulic press, achieving a crosslink density corresponding to a torque increment ΔS’ of 22–25 dNm measured on a moving die rheometer per ASTM D2084. The compound must not be stored in direct contact with secondary amines or ammonia fumes, as ligand exchange degrades the sulfenamide bond prior to vulcanization, generating an unacceptably high room-temperature Mooney viscosity increase of more than 35 units within 48 hours. Final rubber articles include calendered belt skim layers for passenger-car radial tyres and fire-resistant conveyor belts compliant with ISO 340.

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    Certification & Compliance
    More Introduction

    2-(Dimethylaminomethyl)-4-thiazolemethanol — supplied almost exclusively as the hydrochloride salt, CAS 6278-72-4, molecular formula C₇H₁₂N₂OS·HCl, molecular weight 208.71 g·mol⁻¹ — serves as a heterocyclic building block in the synthesis of functionalized thiazoles for medicinal chemistry and life science research. The free base is an oil at ambient temperature; salt formation with hydrogen chloride yields a white to off-white crystalline solid that can be handled and weighed with substantially greater accuracy in moisture-controlled environments. The molecule assembles a 4-hydroxymethyl-substituted thiazole core and a dimethylaminomethyl side chain at the 2-position, creating a bifunctional reactivity profile: the primary alcohol participates in esterification, etherification, and oxidation sequences, while the tertiary amine permits quaternization, N-oxide formation, and coordination to soft Lewis acids.

    Why does this tertiary-amine architecture exhibit divergent behavior compared to 2-aminomethyl-4-thiazolemethanol?

    Replacement of the primary amine with a dimethylated tertiary center eliminates hydrogen-bond donor capacity at the exocyclic nitrogen, reduces the pKₐ of the conjugate acid by approximately 1.0–1.5 log units (calculated pKₐ ≃ 7.8 versus ∼9.2 for the primary amine analog), and markedly increases solubility in moderately polar organic solvents such as ethyl acetate and dichloromethane. In practice, this difference manifests during extractive work-up: while the primary amine partitions preferentially into aqueous acid, the tertiary amine hydrochloride remains extractable into ethyl acetate above pH 6.5, simplifying isolation after reductions or nucleophilic substitutions that involve the 4-methanol group. The dimethylamino group also suppresses formation of Schiff-base by-products when the alcohol is oxidized to the corresponding aldehyde — a pathway that plagues the primary amine derivative due to rapid intramolecular imine cyclisation. For downstream Mannich-type reactions the tertiary amine can be quaternized in situ with methyl iodide in acetone at 0–5 °C to generate a permanently charged ammonium intermediate that directs electrophilic aromatic substitution exclusively to the thiazole 5-position.

    Specification profile for cGMP-compliant hydrochloride batches

    Bulk material destined for use as a regulatory starting material or advanced intermediate is controlled against the monograph in the table below. All methods are validated according to ICH Q2(R1) and executed under ISO 9001:2015-certified quality systems.

    ParameterMethod / ReferenceAcceptance Criterion
    AppearanceVisual inspection, Ph.Eur. 2.2.1White to off-white crystalline powder, free from visible contamination
    Identification (IR)KBr dispersion, Ph.Eur. 2.2.24Spectrum concordant with reference standard; characteristic N–H+ stretch at 2400–2600 cm⁻¹
    Assay (non-aqueous titration)Potentiometric, USP <541>98.5%–101.5% on anhydrous, solvent-free basis
    Water contentKarl Fischer coulometry, USP <921> Method Ic1.0% w/w
    Purity (HPLC)Reverse-phase C18, 150 × 4.6 mm, 5 µm; mobile phase phosphate buffer pH 3.0/MeCN (80:20); 254 nm97.0% area (excluding counterion and void volume peaks)
    Residual solventsHeadspace GC-FID, USP <467> Procedure AIsopropanol ≤ 1000 ppm; methylene chloride ≤ 60 ppm; toluene ≤ 89 ppm
    Sulfated ashPh.Eur. 2.4.140.1%
    Heavy metalsICP-MS after microwave digestion, USP <233>Pd ≤ 5 ppm, Cu ≤ 10 ppm, Fe ≤ 15 ppm

    Out-of-specification results for water content (≥ 1.5%) have been traced on manufacturing campaigns to inadequate nitrogen purging during vacuum tray drying at 40 °C / 10 mbar. A terminal drying step of 24 h at 45 °C under oil-sealed rotary-vane vacuum is standard operating procedure; residual moisture above 0.8% correlates with decreased stability in subsequent N-alkylation reactions using non-aqueous bases.

    The hydrochloride salt is hygroscopic and exhibits a critical deliquescence point near 68% relative humidity at 25 °C. Containers opened outside of glovebox environments with dew points below –30 °C must be back-flushed with dry argon and re-sealed with a molecular sieve desiccant pack. No excipient or stabiliser is blended; the product is supplied as 100% active compound.

    Stability under ICH Q1A(R2) accelerated conditions and incompatible chemical systems

    Stress testing at 40 ± 2 °C / 75 ± 5% RH over 6 months in low-density polyethylene double-bagged secondary containment shows 0.4% absolute purity loss by HPLC, with the primary degradant identified by LC-MS as the thiazole N-oxide (m/z +16 amu). No significant change in assay or water content is observed through 12 months at long-term storage conditions (25 ± 2 °C / 60 ± 5% RH). The compound should not be co-milled or formulated with strong oxidizing agents (peracids, Caro’s acid, nitric acid at concentrations >10%), as rapid exothermic decomposition accompanied by gas evolution has been recorded in reaction calorimetry (RC1e, heat flow >500 W·L⁻¹ at dosing rates exceeding 0.5 mL·min⁻¹). Reactions with acid chlorides or sulfonyl chlorides in the absence of a tertiary amine scavenger generate hydrogen chloride, which catalyzes cleavage of the thiazole ring; stoichiometric control of the base (≥ 2.2 equivalents of triethylamine or Hünig’s base) is mandatory.

    Comparative physicochemical profile against structurally related 4-thiazolemethanols

    CompoundCASMolecular weight (g·mol⁻¹)mp (°C, DSC onset)LogD (pH 7.4, calc.)Key synthetic limitation
    4-Thiazolemethanol7033-31-4115.1571–730.12Poor regioselectivity in electrophilic substitution
    2-Methyl-4-thiazolemethanol7403-34-7129.1856–580.68Benzylic alcohol oxidation prone to over-oxidation
    2-Aminomethyl-4-thiazolemethanol13737-60-1144.2094–96 (dec.)–1.11Intramolecular Schiff-base formation limits shelf-life
    Target compound (as HCl)6278-72-4208.71185 ± 2 (dec.)–0.45Moisture sensitivity necessitates sealed storage

    The target hydrochloride offers an intermediate LogD that balances aqueous solubility (>50 mg·mL⁻¹ in deionized water at 20 °C) with adequate permeability in Caco-2 monolayer assays (apparent Papp >5 × 10⁻⁶ cm·s⁻¹ in published screening panels for structurally related thiazole carriers). This profile makes it a viable precursor for prodrug constructs where the dimethylamine group can be functionalized as a carbamate or amidine without compromising the solubility of the intermediate.

    When deployed as a ligand for palladium-catalyzed cross-coupling, the tertiary amine does not coordinate Pd(II) strongly enough to poison the catalytic cycle — a documented problem with the primary amine analog that requires in situ Boc protection. Suzuki-Miyaura coupling of the 4-hydroxymethyl derivative (after conversion to the 4-bromomethyl analog with PBr₃) proceeds with ≥85% conversion by GC-MS under standard Pd(PPh₃)₄ / K₂CO₃ conditions in dioxane/water at 80 °C. For C–H activation campaigns, the dimethylaminomethyl group serves as a directing moiety, enabling ortho-arylation at the thiazole 5-position with aryl iodides in the presence of Pd(OAc)₂ and AgOAc, as described in literature precedent for dimethylaminomethyl-substituted heterocycles.

    On a 50 L pilot-plant scale, synthesis of the compound via the Mannich reaction of 4-thiazolemethanol with formaldehyde and dimethylamine hydrochloride in acetic acid achieves isolated yields of 72–85% after recrystallization from isopropanol/water (4:1 v/v). The major process-related impurity is the bis-adduct arising from a second Mannich condensation at the 5-position; this impurity is controlled to ≤ 1.5% by holding the reaction temperature at 15 ± 2 °C and limiting the formaldehyde stoichiometry to 1.05 equivalents. Stripping residual acetic acid to <50 ppm in the final dried cake requires two azeotropic distillations with toluene; failures to reduce acid below this threshold have produced off-specification material owing to anomalous titration endpoints.

    Safety data sheet classifications under EC No. 1272/2008 (CLP) for the salt include Skin Irrit. 2 (H315), Eye Irrit. 2 (H319), and STOT SE 3 (H335). Process risk assessments for kilo-lab and larger batches identify the fine dust fraction (<10 µm) as a respiratory irritant; engineering controls must maintain airborne concentrations below the occupational exposure band of 1 mg·m⁻³ (inhalable fraction). Waste streams containing the compound are classified as non-halogenated organic process residues and are incinerated at 1100 °C with a residence time ≥ 2 s under EU Directive 2010/75/EU. No biocidal or food-contact applications are supported; the substance is registered exclusively under REACH as an intermediate under strictly controlled conditions according to Article 17/18 of Regulation (EC) No 1907/2006.