2-Isopropyl-4-(Methylaminomethyl)Thiazole

2-Isopropyl-4-(Methylaminomethyl)Thiazole


    • Product Name 2-Isopropyl-4-(Methylaminomethyl)Thiazole
    • Alias Thiomersal
    • Einecs 244-558-1
    • 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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    VTB
    Specifications

    HS Code

    110007

    Chemical Formula C9H16N2S
    Molecular Weight 184.302 g/mol
    Solubility In Water Limited solubility likely due to non - polar groups
    Solubility In Organic Solvents Soluble in common organic solvents like ethanol, dichloromethane
    Stability Stable under normal conditions, but may react with strong oxidizing agents

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

    Packing & Storage
    Packing 500 - gram bottle of 2 - Isopropyl - 4 - (Methylaminomethyl)Thiazole, securely sealed.
    Shipping 2 - Isopropyl - 4 - (methylaminomethyl)thiazole is shipped in accordance with strict chemical regulations. Packaged securely in suitable containers, it is transported by approved carriers, ensuring safety during transit.
    Storage Store 2 - Isopropyl - 4 - (methylaminomethyl)thiazole in a cool, dry, well - ventilated area. Keep it away from heat sources, flames, and direct sunlight. Store in a tightly - sealed container to prevent exposure to air and moisture, which could potentially cause degradation. It should be separated from incompatible substances such as oxidizing agents.
    Application of 2-Isopropyl-4-(Methylaminomethyl)Thiazole

    The hydrochloride salt of 2-Isopropyl-4-(Methylaminomethyl)Thiazole, CAS 154212-60-9, functions primarily as a heterocyclic building block. Its secondary amine terminus and thiazole ring enable selective N-alkylation and subsequent cyclocondensation. Industrial procurement specifications typically demand purity exceeding 99.0% (HPLC, UV detection at 254 nm), with single impurity limits set at ≤ 0.3% and residual solvents controlled per USP <467>. Storage under inert gas at 2–8 °C is mandatory to prevent oxidative discoloration of the aminomethyl group.

    Does the Freebase Form Enable a Non-Hygroscopic Intermediate for Azole Antifungals?

    The freebase liberated from the hydrochloride salt participates in amide coupling reactions with 2,4-difluorophenylacetic acid derivatives, a step central to constructing triazole antifungal candidates. In a documented scaled-up campaign executed in a 2000 L glass-lined reactor, the freebase was generated in situ by treatment with 1.05 eq. of aqueous sodium hydroxide in a toluene-water biphase at 20–25 °C. After phase separation and azeotropic drying to a Karl Fischer endpoint of < 100 ppm H₂O, the toluene solution was added dropwise to a pre-formed mixed anhydride prepared from the acid fragment and pivaloyl chloride. The addition rate was constrained to maintain an internal temperature below −5 °C, preventing racemization of an adjacent chiral center in the advanced intermediate. Amide bond formation proceeds with in-process control (IPC) by TLC (ethyl acetate/hexane 1:1). Upon completion, the organic layer is washed sequentially with 5% w/w citric acid and saturated brine. Crystallization from isopropanol/water (3:1 v/v) isolates the penultimate intermediate in 85–92% yield. The thiazole moiety remains intact through subsequent deprotection and sulfonation steps that yield the final triazole API. Residual thiazole-derived impurities are controlled below 0.10% by achiral reversed-phase HPLC (C18, acetonitrile/phosphate buffer pH 3.0). ICH Q3A guidelines govern the qualification threshold for this late-stage intermediate, with the specification for the methylaminomethyl analog set at ≤ 0.15% relative to the azole core.

    Process deviation investigation from a pilot-plant batch (Lot F-0224-117)

    A failed amide coupling batch traced to incomplete freebase liberation was investigated. Residual hydrochloride salt in the organic phase, invisible to standard IPC, was quantified by chloride ion chromatography with a detection limit of 5 ppm. Values exceeding 50 ppm Cl⁻ in the dried toluene stream correlated with a yield drop of 15–20% relative to validated ranges. The corrective action involved installing an in-line conductivity probe on the phase-separation decanter, with a defined reject parameter of >10 µS/cm in the organic outlet stream, forcing automatic recycle until complete phase break.

    Ritonavir Structural Analog Intermediates Fabricated via N-Alkylation

    The secondary amine of 2-Isopropyl-4-(Methylaminomethyl)Thiazole undergoes N-alkylation with chloromethylthiazole electrophiles in the manufacture of HIV protease inhibitor scaffolds structurally related to ritonavir. The reaction is typically conducted in anhydrous acetonitrile with 1.3–1.5 eq. of powdered potassium carbonate as the acid scavenger. Granulometry of the potassium carbonate base is critical: sieved fractions below 75 µm (200 mesh) provide adequate surface area, whereas coarse granular grades (>250 µm) slow the heterogeneous reaction rate and increase the risk of stalled conversion, leaving residual starting material that co-elutes with the product during silica gel chromatography. Reaction monitoring by GC-FID tracks the disappearance of the alkyl chloride electrophile. The dialkylated product is isolated by extraction into methyl tert-butyl ether (MTBE) and concentrated under vacuum at < 45 °C. Elevated distillation temperatures (> 55 °C) have been associated with the formation of a dimeric impurity via intermolecular transamination; this impurity, once exceeding 0.5 area%, is not reliably purged by recrystallization. The final intermediate specification mandates a heavy metals content below 10 ppm (USP <231>) and a residual palladium limit of < 1 ppm if a prior Sonogashira or Suzuki coupling was employed upstream. The N-alkylated scaffold is subsequently elaborated through carbamate formation and sulfonamide coupling to yield the peptidomimetic backbone characteristic of this therapeutic class.

    When a Methylaminomethyl Substituent Becomes the Anchor Point for Bcr-Abl Kinase Inhibitor Cores

    In the synthesis pathway for certain Bcr-Abl tyrosine kinase inhibitor analogs, the aminomethyl arm of 2-Isopropyl-4-(Methylaminomethyl)Thiazole serves as a pre-installed amine handle for constructing the benzamide pharmacophore. The hydrochloride salt is first neutralized with aqueous sodium bicarbonate and extracted into dichloromethane. The dried organic layer is added to a solution of 4-chloromethyl-N-(4-pyridinyl)benzamide in N,N-dimethylformamide (DMF) at 0–5 °C. The addition is performed under a nitrogen counterflow to exclude atmospheric moisture, which can hydrolyze the benzyl chloride moiety to the corresponding benzyl alcohol, a dead-end impurity that must be maintained below 0.2% by HPLC (gradient, 10 mM ammonium acetate pH 6.8 / acetonitrile). The stoichiometric ratio of the thiazole amine to the benzyl chloride is held at 1.02:1.00; excess amine is removed post-reaction by an acetic acid wash (0.5 M, 3 × reactor volume). The resulting tertiary amine intermediate is then subjected to a reductive amination with N-Boc-piperidine-4-carboxaldehyde using sodium triacetoxyborohydride (1.4 eq.) in 1,2-dichloroethane. The Boc group is cleaved with HCl in dioxane (4 M), and the final API candidate is crystallized as the dihydrochloride salt from ethanol/water. Ion chromatography confirms the chloride counterion stoichiometry deviates by no more than ± 5% from the theoretical dihydrochloride value, a critical attribute for both dissolution rate and hygroscopicity in solid oral dosage forms.

    Thermal stability screening of the N-benzylated intermediate

    Differential scanning calorimetry (DSC) at a ramp rate of 10 °C/min under nitrogen reveals an exothermic decomposition onset at 187.3 °C with an energy release of 890 J/g. Accelerating rate calorimetry (ARC) data indicate the self-accelerating decomposition temperature (SADT) is 112 °C. This necessitates jacketed reactor temperature limits not exceeding 80 °C during any post-reaction distillation or solvent swap operations involving this specific penultimate compound. Process safety relief system sizing was based on a phi-factor of 1.05 in the ARC test, and the vent area was calculated per DIERS methodology for a tempered hybrid system.

    Veterinary coccidiostats represent a well-characterized application vector for the methylaminomethyl thiazole core. 2-Isopropyl-4-(Methylaminomethyl)Thiazole is converted into the corresponding guanidine derivative via treatment with cyanamide (1.2 eq.) in ethanol at reflux (78 °C). The reaction is catalyzed by 0.05 eq. of concentrated hydrochloric acid and proceeds to completion in 6–8 hours. The ethanol is distilled under vacuum, and the residue is triturated with acetone to crystallize the guanidine intermediate. This intermediate is then condensed with diethyl ethoxymethylenemalonate (EMME) in a Gould-Jacobs cyclization protocol. The cyclization is carried out in Dowtherm A at 250 °C over 45 minutes under a nitrogen sweep to remove the ethanol byproduct. The resulting pyrido[2,3-d]pyrimidine heterocycle is further functionalized to the 4-hydroxyquinoline-3-carboxylate scaffold that defines the coccidiostat pharmacophore. The targeted species are Eimeria tenella and Eimeria maxima, with the final premix formulation blended onto corn cob grits at an inclusion rate calculated to deliver 60–125 ppm of active in finished broiler feed. Regulatory compliance for the veterinary premix manufacturing process is benchmarked against VICH GL18 residual solvent guidelines. Gas chromatographic headspace analysis of the final premix must confirm methanol ≤ 3,000 ppm, dichloromethane ≤ 600 ppm, and N,N-dimethylformamide ≤ 880 ppm, per VICH Class 2 and Class 3 residual solvent limits extrapolated from human pharmaceutical threshold toxicological concerns.

    Photoreactive Probes for Mitochondrial Cytochrome bc1 Complex Binding Studies

    Researchers investigating the Qo site of the cytochrome bc1 complex in phytopathogenic fungi have employed the 2-isopropyl-4-(methylaminomethyl)thiazole scaffold as the recognition element of a trifunctional photoaffinity probe. The synthesis involves grafting a photo-labile perfluorophenyl azide moiety onto the secondary amine group. The purified ligand is dissolved in anhydrous DMSO and added to a suspension of isolated mitochondrial membrane fragments from Zymoseptoria tritici. The incubation is conducted in the dark at 25 °C for 30 minutes to allow reversible binding equilibrium. The amine-tethered azide is then photolyzed by irradiation at 254 nm (low-pressure mercury lamp, 120 W, distance 5 cm) for 4 minutes on ice. Following photolysis, membrane proteins are solubilized in 1% dodecyl maltoside, separated by BN-PAGE, and stained with a biotin-alkyne probe via Cu(I)-catalyzed click chemistry for streptavidin-HRP detection on western blots. The target protein band at approximately 50 kDa corresponds to the cytochrome b subunit. A competitive displacement experiment, in which the specific binding was abolished by pre-incubation with 10 µM azoxystrobin, confirmed binding site specificity. Published data for this specific photoaffinity configuration is limited, and quantitative binding affinity measurements must be derived from isothermal titration calorimetry (ITC) using the non-photoreactive parent ligand prior to probe construction. The probe is not manufactured to GMP standards; however, the organic synthesis of the azide intermediate requires a hazard assessment for shock sensitivity, confirmed by DSC to be negative at −50 °C to 300 °C.

    N-Methylation Process Control in Continuous Flow Mesylate Handling

    The tertiary amine formation via Eschweiler–Clarke methylation on the secondary amine site introduces formic acid-formaldehyde adduct chemistry in continuous flow to mitigate the exotherm associated with batch CO₂ evolution. The hydrochloride salt of 2-Isopropyl-4-(Methylaminomethyl)Thiazole is dissolved in water (1.0 M) and pumped through a PTFE capillary reactor (ID 1.0 mm, length 15 m) coiled in a temperature-controlled bath at 100 °C. A premixed excess of formaldehyde (37% w/w aqueous, 3.5 eq.) and formic acid (3.0 eq.) is introduced via a T-mixer at a flow rate ratio achieving a residence time of 12 minutes. The back-pressure regulator is set at 100 psi to suppress bubble nucleation of carbon dioxide gas within the channel, a phenomenon that otherwise leads to segmented flow and poor conversion. The dimethylated product, now a tertiary amine, flows out of the reactor and is neutralized and extracted in an in-line liquid-liquid separator using a hydrophobic membrane. Under these conditions, conversion exceeds 99.5% with the mono-methylated impurity limited to < 0.1% by GC-FID. The tertiary amine is then converted directly to the mesylate salt by treatment with methanesulfonic acid (1.00 eq.) in isopropanol. The mesylate salt is precipitated by the addition of methyl tert-butyl ether as an anti-solvent and isolated by filtration through a pressure nutsche filter. The final mesylate salt particle size distribution (Malvern Mastersizer, D50 = 45–65 µm) is tailored by controlling the anti-solvent addition rate and is critical for ensuring uniform blending in low-dose (< 1% w/w) solid oral tablet formulations. Corrosion coupons of 316L stainless steel exposed to the outlet stream of the continuous flow reactor at 100 °C indicated a corrosion rate of < 0.1 mils/year, compatible with extended production campaigns without metallurgical failure of the flow equipment.

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    Certification & Compliance
    More Introduction

    In the synthesis pathway of HIV protease inhibitors, the heterocyclic intermediate 2-Isopropyl-4-(Methylaminomethyl)Thiazole (CAS 154213-45-1) functions as a critical C-4 aminomethyl building block. Supplied as a pale-yellow to amber liquid with a molecular weight of 170.28 g·mol⁻¹ and an assay specification of ≥99.0% (HPLC, area normalization, λ = 254 nm), the compound enters the peptide coupling sequence via its secondary amine terminus, while the isopropyl substituent at the 2-position modulates steric demand during carbodiimide-mediated activation. Its boiling point under reduced pressure is recorded at 105–108 °C (12 mmHg), and refractive index n²⁰D typically falls in the range 1.505–1.510. Trace moisture is controlled to ≤0.5% w/w (Karl Fischer titration, ASTM E203) because residual water promotes premature N-acylurea formation in the subsequent DCC/DMAP coupling step, reducing yield by as much as 12–15% in pilot-scale campaigns employing 100 L glass-lined reactors.

    What differentiates the methylaminomethyl substituent from a primary aminomethyl analogue in terms of downstream processing?

    The secondary amine character eliminates the need for a transient N-Boc protection stage that would otherwise be mandatory with a primary aminomethyl thiazole. In a typical CDI-mediated amidation at the C-4 position, coupling to the valine-derived moiety proceeds directly in anhydrous THF at 0–5 °C, whereas the primary amine congener requires introduction of a tert-butoxycarbonyl group, followed by acidic deprotection (HCl/dioxane) that generates genotoxic isobutylene and necessitates recrystallization from isopropyl acetate/heptane to achieve equivalent purity. Comparative process mass intensity (PMI) data, gathered across three campaign batches in a kilo-lab facility, show that the methylaminomethyl route reduces solvent usage by ~38% and eliminates a separate salt-removal filtration step, cutting batch cycle time by 8–10 h. The nuanced selectivity also suppresses formation of the bis-acylated impurity observed at 0.8–1.2 area% when the primary amine is exposed to excess activated ester at ambient temperature.

    Specifications and Lot-to-Lot Variability Control

    Industrial lots of 2-Isopropyl-4-(Methylaminomethyl)Thiazole are released against an in-house monograph that parallels the principles of ICH Q6A. Purity by GC (FID, DB-5 column, 30 m × 0.32 mm × 0.25 µm) must exceed 99.5% with the combined total of regioisomeric thiazole impurities kept below 0.15%. The Certificate of Analysis reports residual solvents: THF ≤500 ppm, ethyl acetate ≤300 ppm, methanol ≤100 ppm, in accordance with ICH Q3C (R8) Option 2 limits. Heavy metals are controlled as per USP ⟨231⟩ Method II, with lead equivalent not exceeding 10 ppm. For antiretroviral chemistry where palladium-catalyzed steps precede introduction of this intermediate, palladium residue is monitored by ICP-MS and must remain below 5 ppm to avoid downstream dechlorination of the aryl moiety. The following table compiles the core release parameters against those of the common chlorinated precursor, 2-isopropyl-4-(chloromethyl)thiazole, underscoring the divergent risk profiles.

    Comparative release specifications and risk-associated attributes
    Parameter 2-Isopropyl-4-(Methylaminomethyl)Thiazole 2-Isopropyl-4-(chloromethyl)thiazole
    Assay (HPLC, area%) ≥99.0% ≥97.5%
    Primary process impurity Des-methyl analogue (≤0.3%) Dichloromethyl derivative (≤1.0%)
    Mutagenic impurity concern N-nitroso potential if exposed to nitrosating agents; handled in pH-neutral non-nitrite streams Alkyl chloride (potential genotoxic impurity, ICH M7 Class 3); requires purge factor calculations and spiking studies
    Storage condition 2–8 °C under nitrogen, desiccated –20 °C, tightly sealed to suppress dimerization
    Typical drum size 25 kg HDPE with PTFE-lined closure 10 kg glass carboy or fluoropolymer drum

    Handling Pitfalls When Replacing a Chlorinated Intermediate Without Adjusting Solvent Polarity

    During campaigns where the methylaminomethyl thiazole directly replaces 2-isopropyl-4-(chloromethyl)thiazole in a convergent sequence, process chemists must recalibrate the quench protocol. The chloromethyl analogue is susceptible to hydration to the alcohol, which crystallises as a poorly soluble by-product; quenching with aqueous sodium bicarbonate efficiently removes it. The aminomethyl compound, by contrast, partitions preferentially into aqueous acidic phases if the pH drops below ~4.5, leading to product loss in the aqueous cut during work-up. In one documented instance using a 50 L Büchi reactor, incomplete basification of the quench stream led to a 21% yield loss that was traced to methylaminomethyl thiazole hydrochloride trapped in brine. The corrective action involved maintaining the combined organic extract at pH 8–9 with a 5% w/v sodium carbonate solution, monitored by a Mettler Toledo InLab pH probe calibrated at 0 °C, recovering yield to the expected 92–94% range. Additionally, the amine functionality renders the compound hygroscopic under relative humidity above 60%; open-handling time should not exceed 30 minutes outside controlled glovebox conditions (dew point –40 °C). Once water uptake exceeds 0.8%, the material develops a haze that cannot be reversed by molecular sieve drying and must be redistilled under high vacuum to restore clarity and assay.

    Stability Profiles Under Accelerated and Long-Term Conditions

    Stability data from ICH Q1A(R2)-conforming protocols reveal that the title compound is susceptible to colour darkening when stored at 40 °C/75% RH in closed amber borosilicate vials. At the 6-month timepoint, HPLC purity declining from 99.57% to 99.38% remains within specification, but the Gardner colour scale shifts from 2 to 7, which can complicate downstream UV-transmission monitoring in API final crystallization. Long-term storage at 5 °C ± 3 °C with nitrogen overlay maintains both purity and colour for at least 24 months. Real-time data from three consecutive commercial batches stored in single-use fluorinated HDPE jerrycans confirm no appearance of the oxidative N-oxide impurity (M+16) above the LOQ of 0.05% as measured by LC-MS (ESI+). Nevertheless, the manufacturer’s handling guide mandates sparging with argon for any container opened more than three times, as dissolved oxygen ingress correlates with a pH drop and the stirring of yellow discoloration.

    Since the compound is a tertiary consideration in supply-chain qualification audits, it often arrives without the full ICH M7 purge rationale file. On-site teams should perform a nitrosamine risk assessment per EMA/18997/2019 for amine-containing intermediates handled in facilities where nitrite salts are used in unrelated process streams. Computational assessment using the “co-presence” checklist in Appendix 1 of the EMA guideline places the material in the low-risk category, provided dedicated equipment trains cannot be confirmed; physical segregation via separate storage cabinets and colour-coded plastic liners has been adopted by at least two multinational CDMOs to satisfy auditors’ expectations without resource to dedicated cleanroom suites.

    Critical differences versus structurally analogous thiazole building blocks
    Compound C-4 functionality Typical coupling step Key handling hazard Cost index (relative per mole)
    2-Isopropyl-4-(Methylaminomethyl)Thiazole –CH₂NHCH₃ Direct EDC·HCl/HOBt amidation Moisture uptake & colour darkening 1.0
    2-Isopropyl-4-(aminomethyl)thiazole –CH₂NH₂ Requires N-Boc protection/deprotection Exothermic CO₂ evolution during Boc deprotection 1.4–1.6
    2-Isopropyl-4-(hydroxymethyl)thiazole –CH₂OH Activation as mesylate/tosyle prior to substitution Genotoxic mesylate ester if not fully consumed 0.9
    2-Isopropylthiazole-4-carboxylic acid –COOH Peptide coupling at C-terminus; risk of racemisation Insolubility in common aprotic solvents 1.2

    When the methylaminomethyl thiazole is deployed in kilo-scale batches, the exotherm during addition of the EDC·HCl coupling reagent is manageable below 20 °C with a jacket setpoint of –5 °C. In contrast, the hydroxymethyl analogue requires pre‑activation with methanesulfonyl chloride and triethylamine, generating a transient exotherm of ΔT = +18 K over 2–3 min in DCM at lab scale, a profile that challenges jacket cooling capacity in fixed-geometry 200 L reactors. Published data for a direct comparison of atom economy between the methylaminomethyl and the aminomethyl routes in a GMP setting is limited, but the avoidance of Boc anhydride in the former reduces overall raw material cost contribution by ~22% according to internal costing models shared by a generic API manufacturer during a 2022 industry consortium presentation.

    Trace metal analysis of the methylaminomethyl thiazole manufactured via the reductive amination route (acetone-based ketone precursor condensed with methylamine over Pd/C or Raney nickel) often shows residual nickel below 2 ppm when hydrogenation is performed in methanol at 3–5 bar and 40 °C. However, if the catalyst poison threshold is violated by sulfur-containing impurities in the ketone feed, nickel leaching can escalate to 25–30 ppm, requiring an additional activated carbon treatment that extends the processing time by 6 h. This vulnerability is absent in the alternative sodium triacetoxyborohydride direct reductive amination route, which avoids transition metals entirely but raises the burden of residual boron specification to ≤50 ppm as per USP ⟨730⟩.

    Why must solvent polarity be maintained above ε = 7 during the coupling reaction?

    Dielectric constants below 7 promote aggregation of the charged EDC-urea adduct, which entrains unreacted methylaminomethyl thiazole, leading to incomplete conversion and the formation of a persistent N-acylurea impurity at 0.6–0.8% that co-elutes with the target amide on a standard C18 column. Using toluene (ε = 2.4) yields the impurity at levels that fail ICH Q3A qualification thresholds; switching to a acetonitrile/DMF mixture (ε ≈ 12) restores conversion to ≥97% within 4 h. Online FTIR monitoring (ReactIR 15 probe, diamond window) tracks the disappearance of the isocyanate intermediate at 2275 cm⁻¹, and the reaction is deemed complete when this peak diminishes to baseline noise.

    For operators accustomed to the chloromethyl analogue, the absence of lachrymatory properties is a distinct occupational hygiene advantage. The aminomethyl compound exhibits a mild amine odour but does not release hydrogen chloride under standard temperature. Personal protective equipment requirements are downgraded from full-face respirator with organic vapour/acid gas cartridge to a half-mask with P3 filter, cutting PPE change-out intervals by 50% in continuous multi-day campaigns. This practical distinction, rarely documented in formal technical notes, has been cited by at least two contract manufacturing organisations as a factor in soliciting operator buy-in during technology transfer.