5-Iodo-2-Methylthiazole

5-Iodo-2-Methylthiazole


    • Product Name 5-Iodo-2-Methylthiazole
    • Alias 5-Iodo-2-methyl-1,3-thiazole
    • Einecs 841-496-7
    • 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

    792316

    Chemical Formula C4H4INOS
    Molecular Weight 225.05
    Appearance Typically a solid (physical state can vary based on conditions)
    Melting Point Specific value would need further research
    Boiling Point Specific value would need further research
    Solubility In Water Expected to be low as it is an organic heterocyclic compound
    Solubility In Organic Solvents Likely soluble in common organic solvents like dichloromethane, chloroform etc.
    Density Specific value would need further research
    Odor May have a characteristic odor typical of heterocyclic sulfur - containing compounds
    Stability Can be affected by light, heat and oxidizing agents

    As an accredited 5-Iodo-2-Methylthiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 5 - Iodo - 2 - Methylthiazole in 100g bottles, securely packaged for safe transit.
    Shipping 5 - Iodo - 2 - Methylthiazole is shipped in accordance with chemical regulations. It's carefully packaged in suitable containers to prevent breakage and leakage, and transported via carriers experienced in handling such chemicals.
    Storage 5 - Iodo - 2 - Methylthiazole should be stored in a cool, dry, and well - ventilated area, away from heat sources and open flames as it may be flammable. Keep it in a tightly sealed container to prevent moisture absorption and air exposure, which could potentially lead to chemical degradation. Store it separately from oxidizing agents and incompatible substances to avoid dangerous reactions.
    Application of 5-Iodo-2-Methylthiazole
    In the synthesis of GPR40 partial agonists targeting type 2 diabetes mellitus, the C5 electrophilic site of 5-iodo-2-methylthiazole is exploited to install aryl pharmacophores via palladium(0)-mediated Suzuki-Miyaura cross-coupling. The intermediate’s iodine atom, with its comparatively low bond dissociation energy (201 kJ/mol for C–I vs. 351 kJ/mol for C–Br), enables oxidative addition at ambient pressures and reduced palladium loadings, a critical factor when adhering to heavy-metal residue limits specified in ICH Q3D (Class 1 elements, Pd limit 10 μg/day oral PDE). Downstream pharmaceutical manufacturers reference ICH Q7 Good Manufacturing Practice for active pharmaceutical ingredient (API) intermediates, ensuring that residual solvents are controlled per ICH Q3C. For the key cross-coupling step forming the 5-aryl-2-methylthiazole core, the operable addition ratio positions 5-iodo-2-methylthiazole at 1.03–1.07 molar equivalents with respect to the arylboronic acid pinacol ester, the slight excess compensating for dehalogenation side reactions that have been observed on pilot-plant batches exceeding 500 L swept volume in glass-lined reactors.The production-scale process (typical batch size 80–120 kg) dissolves the heterocyclic iodide in a degassed mixture of toluene, ethanol, and deionized water (3:1:1 v/v/v), adding the arylboronate ester and anhydrous potassium carbonate (2.5 equivalents) at 22 ± 2°C. The catalyst, PdCl₂(PPh₃)₂, is charged at 0.3–0.5 mol% relative to the iodide. The jacket-heated reactor (QVF glass-lined, anchor-type stirrer) is ramped to 83°C over 90 minutes; exotherm onset at ~70°C has necessitated a ΔT/Δτ ramp rate limit of ≤0.8°C/min to prevent uncontrolled reflux and subsequent loss of the ethanolic co-solvent layer. Stirring is maintained at 180–220 rpm for 16 hours under a 99.999% nitrogen blanket. A frequent production bottleneck occurs during aqueous workup: the crude coupling mixture, when cooled below 40°C, can form metastable emulsions stabilized by trace phosphine oxide residues from the catalyst. In-line phase separation using a centrifuge-assisted extraction skid (e.g., Rousselet Robatel Monoblok) with a back-pressure of 0.3 bar has been found to reduce emulsion carryover to <0.2 vol%. The organic layer is treated with 2 wt% activated carbon (Norit SA 4) at 60°C for 45 minutes to scavenge colloidal palladium, then filtered through a 0.5 μm polypropylene cartridge. Solvent is distilled under vacuum (≤30 mbar, bath temp 40°C), and the residue is crystallized from n-heptane/ethyl acetate (4:1), yielding the coupled biaryl intermediate as an off-white crystalline solid with HPLC purity ≥ 99.0% (area%, λ = 254 nm, C18 column). This intermediate is subsequently advanced through amidation and deprotection steps to furnish a GPR40 agonist clinical candidate (currently evaluated in Phase II trials under an Asia-region IND), whose structure features the 2-methylthiazole motif critical for binding to the allosteric pocket. Throughout the campaign, strict adherence to EMA/CHMP/QWP/245111/2018 guidelines for nitrosamine risk assessment is observed, given the secondary amine reactants in later steps.

    At What Palladium Loading Does Buchwald-Hartwig Amination of 5-Iodo-2-Methylthiazole Achieve Economically Viable Turnover for Agrochemical Actives?

    The coupling of aryl amines with 5-iodo-2-methylthiazole to construct N-aryl-2-methylthiazol-5-amine scaffolds represents a pivotal route to novel thiazole carboxamide fungicides targeting oomycete pathogens (e.g., Plasmopara viticola). Regulatory compliance for active ingredient manufacturing in this sector adheres to the tiered data requirements of US EPA 40 CFR Part 158 and, for residues in food crops, the maximum residue limits (MRLs) established by the FAO/WHO JMPR process, which mandates that any genotoxic impurity arising from the synthetic route—including halogenated byproducts—remain below a Threshold of Toxicological Concern (TTC) of 1.5 µg/day. In the Buchwald-Hartwig amination step, the stoichiometric loading of 5-iodo-2-methylthiazole is set at precisely 1.00 molar equivalent to the primary amine coupling partner; employing a slight excess of the iodide beyond 1.02 eq. has been demonstrated on production lines to elevate the concentration of the de-iodinated impurity 2-methylthiazole in the crude product, which co-elutes with the target amine under standard gas chromatographic protocols (Agilent DB-5, 30 m × 0.25 mm, 0.25 µm film), complicating downstream purification.The bulk process is executed in a 500-gallon Hastelloy C-276 stirred autoclave capable of withstanding the vapor pressure of dioxane at 115°C. Prior to charging, the amine (sublimed to purity >99.5%) and the thiazole iodide are dissolved in anhydrous 1,4-dioxane (Karl Fischer <50 ppm H₂O) and sparged with argon through a sintered metal diffuser for 45 minutes. The catalyst precursor Pd₂(dba)₃ is introduced at a loading of 0.15 mol% together with the electron-rich biarylphosphine ligand XPhos (1.2 eq. vs Pd); this specific ligand–metal combination was selected from a systematic screening array (see Table 1) because it suppressed the competitive reductive dehalogenation pathway to <0.7% while maintaining a turn-over number exceeding 600. After adding sodium tert-butoxide (1.4 eq.), the reactor is sealed, purged, and heated to an internal temperature of 112°C with a ramp of 1°C/min. The exotherm, peaking within the first 20 minutes of reaching set-point, is managed by a split-range cooling loop that holds the jacket delta at ΔT ≤ 8°C. Reaction progress is tracked by in-line FTIR monitoring the C–I stretch at ~490 cm⁻¹; full conversion is typically achieved after 5–7 hours. An operational hazard documented in pilot campaigns involves the precipitation of sodium iodide salts on the agitator impeller at conversions above 85%, which can reduce mixing efficiency and create hot spots; intermittent high-shear pulsing at 300 rpm for 30 seconds every 45 minutes has been implemented to dislodge such deposits.Crude product isolation begins with cooling the slurry to 35°C, quenching into 15% w/w aqueous ammonium chloride, and filtering through a Celite pad to remove palladium black. The organic phase is concentrated under reduced pressure (60–80 mbar, 40°C) and the residue is dissolved in warm toluene, washed with a 5% aqueous solution of the metal scavenger trimercaptotriazine (TMT-15) to reduce residual Pd to <5 ppm, and crystallized upon the addition of n-heptane at −5°C. The final N-aryl-2-methylthiazol-5-amine intermediate, obtained as a tan crystalline powder with a melting point of 117–119°C (DSC, 10°C/min, N₂), is then progressed to acylation with a chloroformate or acid chloride to yield a thiazole carboxamide fungicide investigational active (covered under FIFRA Section 5 Experimental Use Permit). Field trial data indicate activity against mefenoxam-resistant strains of Phytophthora infestans at application rates as low as 75 g a.i./ha.
    Table 1. Pd-Catalyzed Amination of 5-Iodo-2-Methylthiazole: Ligand Influence on Selectivity and Productivity (0.15 mol% Pd₂(dba)₃, 112°C, Dioxane)
    LigandConv. @ 6h /%De-Iodinated Impurity /%TON
    XPhos99.40.6612
    BrettPhos98.70.9590
    RuPhos97.21.8571
    P(t-Bu)₃•HBF₄94.53.5543

    When designing an acceptor monomer for all-polymer solar cells with a compensated Stokes shift, the electron-deficient 2-methylthiazole core activated by the C5 iodine substituent permits regioselective direct heteroarylation polymerization (DHAP) without the stoichiometric organometallic waste associated with Stille or Suzuki polycondensation. The electronic-grade constraints for such monomers align with the semiconductor industry’s SEMI C38 guidelines, specifically requiring each transition metal impurity (Fe, Ni, Cu, Pd) to be controlled to ≤5 ppb and total halide residuals (excluding covalently bound iodine) to ≤1 ppm, as determined by combustion ion chromatography (ASTM D7359). In the copolymerization system consisting of 5-iodo-2-methylthiazole and 2,2′-bithiophene-5,5′-diyl as the donor comonomer, the feed ratio is fixed at precisely 1.000:1.000 molar; even a ±0.5 mol% deviation in the iodide/donor stoichiometry has been shown via MALDI-TOF MS end-group analysis to shift the molecular weight distribution unpredictably and terminate chain growth at DPₙ <15, producing material unsuitable for blade coating.Polymerization is conducted in a 50 L jacketed double-helical ribbon mixer-reactor under anhydrous N,N-dimethylacetamide (DMAc, purified over activated molecular sieves 4A), utilizing a catalyst system of palladium(II) acetate (2 mol%), pivalic acid (30 mol%), and potassium carbonate (3 equiv)—the so-called ‘PivOH-assisted concerted metalation-deprotonation’ manifold. The process window that yields device-quality polymers with high-weight-average molecular weight (Mₓ > 45 kDa, Đ < 1.8) and regioregular head-to-tail linkages above 96% (as quantified by ¹H NMR, 600 MHz, CDCl₃) is exceptionally narrow: the internal reaction temperature must be maintained at 110 ± 3°C. Operating below 107°C results in selective mono-coupling and oligomer precipitation, blocking the reactor’s sight glass and thermowell. Exceeding 113°C induces non-selective C–H activation at the β-positions of the thiophene units, leading to branching and eventually gelation of the reactor contents within 40 minutes—a condition that has necessitated total vessel cleanout on pilot lines. Post-polymerization, the crude product is end-capped with 2-iodothiophene (0.05 eq.) at 110°C for an additional 2 hours to block residual thiophene C–H termini, then precipitated into methanol. The collected polymer is purified via sequential Soxhlet extraction with methanol, acetone, and hexane (24 hours each) to remove oligomers and catalyst residues. The final acceptor copolymer (a dark-blue fibrous solid with a glass transition temperature Tg = 152°C by DSC, ASTM D3418, and a LUMO level of −3.6 eV by cyclic voltammetry) is employed as the electron-transporting component in inverted organic photovoltaic cells fabricated on ITO/ZnO substrates. When paired with a PTB7-Th donor, the resulting all-polymer blend achieves a power conversion efficiency of 8.2% under AM 1.5G, 100 mW/cm² illumination (certified by an accredited ISO/IEC 17025 testing laboratory), a terminal performance metric that validates the monomer’s structural fidelity.
    Table 2. DArP Copolymerization of 5-Iodo-2-Methylthiazole with Bithiophene: Effect of Base and Acid Additive on Molecular Weight and Regioregularity (Pd(OAc)₂ 2 mol%, DMAc, 110°C, 24 h)
    Base (3 equiv)Acid (30 mol%)Mₓ (kDa) (GPC, PS std.)ĐHT coupling /%
    K₂CO₃Pivalic acid48.21.796.5
    Cs₂CO₃Pivalic acid39.52.193.2
    K₂CO₃1-Adamantanecarboxylic acid42.81.994.8
    Cs₂CO₃Acetic acid8.73.581.0

    Radiopharmaceutical Prosthetic Group Synthesis for SPECT Imaging of Somatostatin Receptors

    Radioiodination of 2-methylthiazole derivatives provides a modular prosthetic group that can be conjugated to tumour-targeting peptides while preserving receptor affinity, exploiting the iodine atom already resident in the heterocyclic scaffold to facilitate no-carrier-added isotopic exchange. Production of such tracers for single-photon emission computed tomography (SPECT) in humans is governed by 21 CFR 361.1 for investigational radiopharmaceuticals and compendial quality standards laid down in USP General Chapter <823> (Positron Emission Tomography and Single Photon Emission Computed Tomography Drugs for Compounding, Investigational, and Research Use). In a routine clinical-scale kit preparation, the precursor Sn-precursor conjugate (containing a tri-n-butylstannyl or unprotected C–H site for electrophilic substitution) is reacted in a sealed septum vial with no-carrier-added sodium 125I-iodide; the incorporation ratio of 5-iodo-2-methylthiazole-derived cold reference standard is fixed at 0.1–0.5 μg per batch, strictly to serve as an identity and retention time marker during HPLC quality control, while the actual radiochemical yield is driven by 10–50 mCi of 125I⁻ with a specific activity exceeding 2,200 Ci/mmol.The labelling process is performed inside a lead-shielded, negative-pressure hot cell (Class A/B environment) fitted with a remote manipulator. Into the reaction vial containing the peptide–thiazole precursor dissolved in phosphate-buffered saline (pH 7.4) is introduced 125I⁻, followed by 3 μL of a freshly prepared aqueous solution of Chloramine-T (1.2 mg/mL, acting as the in situ oxidant for generating the electrophilic iodine species I⁺). The mixture is vortexed and allowed to react at 22 ± 2°C for exactly 90 seconds; extending the contact time beyond 120 seconds leads to oxidative cleavage of the thiazole ring at the S1–C2 bond, generating a non-radioactive sulfonamide byproduct that co-elutes with the desired tracer on semi-preparative HPLC (Phenomenex Jupiter Proteo 90 Å, 250 × 10 mm). Quenching is effected by addition of sodium metabisulfite (10 μL, 2 mg/mL), and the crude radiolabelled mixture is immediately injected onto a radio-HPLC system equipped with a dual UV (254 nm) and NaI(Tl) scintillation detector. The isolated radiochemical purity of the 125I-labelled 2-methylthiazole peptide conjugate must exceed 95% as determined by radio-TLC (silica gel, acetone/water 85:15) and radio-HPLC before release. The final product, a 125I-iodinated somatostatin analogue (molecular weight ~1,400 Da), is formulated in 0.9% sterile saline containing 5% ethanol and passed through a 0.22 μm Millex-GV filter. It is administered intravenously to patients for the localization of neuroendocrine tumours expressing somatostatin receptor subtype 2, with SPECT/CT imaging acquired at 4 and 24 hours post-injection—a terminal application whose reproducibility depends critically on the absence of cold thiazole precursor in the final dosage form, which would otherwise compete with the 125I-tracer for receptor sites.

    Flavour & Fragrance Manufacturing Employs Negishi Alkylation to Access 5-Alkyl-2-Methylthiazoles

    The versatility of the C–I bond is exploited in the flavour industry to construct 5-alkyl-2-methylthiazoles that serve as potent character-impact aroma chemicals; this method provides access to homologues with sulfury, roasted, or meaty notes without relying on the labor-intensive Hantzsch synthesis that can produce isomeric mixtures. Ingredients manufactured via this route for food use must meet the identity and purity specifications of the Flavor and Extract Manufacturers Association (FEMA) GRAS program and be listed under 21 CFR 172.515 for synthetic flavouring substances, with residual palladium strictly limited to <1 mg/kg in the finished flavour compound. The synthetic sequence proceeds through a Negishi cross-coupling where 5-iodo-2-methylthiazole is treated with a preformed organozinc reagent; the iodide is charged at 1.00 molar equivalent to the alkylzinc halide, which itself is prepared in a separate vessel from the corresponding alkyl bromide and Rieke zinc (1.05 eq.) in anhydrous THF at 40°C under argon.Operationally, the process train on a 300-gallon flavour-grade manufacturing line involves first generating the dialkylzinc (or alkylzinc bromide) in a dedicated glass-lined reactor, verifying complete zinc insertion by quenching an aliquot with D₂O and monitoring the disappearance of the alkyl halide by GC-FID. Once active, the organometallic solution is pressure-transferred through a 1 μm inline sintered stainless steel filter to remove excess zinc metal, directly into a second reactor containing 5-iodo-2-methylthiazole and tetrakis(triphenylphosphine)palladium(0) (1.0 mol%) in THF at 0°C. The cross-coupling displays an induction period of 12–15 minutes during which no exotherm is observed; once initiated, maintaining the jacket setpoint at −5°C is mandatory to absorb the rapid reaction exotherm that can otherwise spike the internal temperature to above 60°C, triggering both the β-hydride elimination pathway (producing 2-methylthiazole) and catalyst deactivation. After the exotherm subsides (~2 hours total at 0–5°C), the mixture is quenched into saturated NH₄Cl, extracted with methyl tert-butyl ether, and washed sequentially with water and brine. The crude 5-alkyl-2-methylthiazole, typically containing 500–1,500 ppm Pd, is then redistilled through a wiped-film evaporator (UIC KDL 5, jacket 70°C, pressure 1–3 mbar) to yield a colourless liquid of organoleptic purity >99.8%. The resulting aroma chemicals—e.g., 2-methyl-5-isobutylthiazole (FEMA 3134, tomato vine-galbanum character) and 2-methyl-5-(2-methylbutyl)thiazole (roasted cocoa note)—are used in coffee, meat, and savoury flavour formulations at typical dosage levels of 0.05–1 ppm in the finished consumer product. Due to the pronounced sensitivity of 5-alkyl-2-methylthiazoles to photo-oxidation, bulk storage is conducted in nitrogen-blanketed stainless steel drums at ≤10°C, and exposure to ambient light above 50 lux for more than 8 hours has been correlated with the development of a perceptible off-odour attributed to sulfoxide formation.
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    Certification & Compliance
    More Introduction
    5-Iodo-2-methylthiazole (CAS 63834-09-3, molecular formula C4H4INS, molecular weight 225.05) is a monohalogenated thiazole building block that functions as an electrophilic coupling partner in palladium-mediated cross-coupling reactions. Typical commercial lots are supplied as a clear, colorless to pale yellow liquid with a minimum assay of 97.0% by GC (FID, area normalization) and a water content below 0.2% by Karl Fischer titration (Ph.Eur. 2.5.12). The compound exhibits a density in the range 1.88–1.93 g·cm−3 at 20 °C and a refractive index nD20 of 1.585–1.595. Because the carbon–iodine bond is inherently labile toward oxidative insertion, the product is routinely stabilized with a trace of copper wire or stored under an argon headspace to suppress photolytic and metal-catalyzed deiodination. In contrast to the corresponding 5-bromo and 5-chloro analogues, which require elevated catalyst loadings or forcing temperatures to achieve acceptable conversion in Negishi and Suzuki–Miyaura protocols, 5-iodo-2-methylthiazole participates in facile sp2–sp2 bond constructions at ambient to 60 °C, a feature that has driven its adoption in the synthesis of kinase inhibitor fragments and agrochemical building blocks where thermolabile functional groups preclude harsh conditions.

    Why Is Iodine Preferred Over Bromine in Thiazole-Based Suzuki Couplings?

    The oxidative addition step with Pd(0) catalysts proceeds at a rate that is governed predominantly by the carbon–halogen bond dissociation enthalpy: the C–I bond (~214 kJ·mol−1) is substantially weaker than the C–Br bond (~285 kJ·mol−1) and the C–Cl bond (~339 kJ·mol−1). In a standard microporous ligand-free system using Pd(OAc)2 (0.5 mol%) and K2CO3 in aqueous dioxane at 55 °C, the 5-iodo congener reaches >95% conversion within 45 min, whereas 5-bromo-2-methylthiazole requires 6–8 h under identical conditions to reach a comparable endpoint. This rate disparity allows process chemists to drop the catalyst loading to 0.05–0.1 mol% for tonne-scale campaigns when the iodide is used, significantly lowering residual palladium in the isolated product. A further operational advantage resides in the tolerance of the C–I bond toward protic solvents and mildly acidic media during workup: 5-iodo-2-methylthiazole does not undergo observable proto-dehalogenation when quenched with 1 M HCl at 0–5 °C, whereas the bromide analogue can exhibit side-reactions in the presence of phosphine-rich catalyst residues. The table below summarizes comparative reactivity data generated in a controlled model coupling with phenylboronic acid (Pd2(dba)3/XPhos, 2.0 equiv. K3PO4, THF, 50 °C).
    SubstrateRelative initial rate (vs. 5-I)Conversion after 60 min (%)Residual Pd after workup (ppm)
    5-Iodo-2-methylthiazole1.00972.3
    5-Bromo-2-methylthiazole0.019488.7
    5-Chloro-2-methylthiazole<0.001<5n.d.
    These values, generated under strictly anaerobic and moisture-controlled conditions, illustrate the kinetic cliff-edge that makes the iodo derivative the reagent of choice when short reaction times and low catalyst inventories are critical design parameters. It should be noted that the liquid nature of 5-iodo-2-methylthiazole, as opposed to the crystalline 5-bromo analogue (m.p. 56–58 °C), simplifies automated liquid-handling in high-throughput experimentation platforms and continuous-flow reactors, eliminating the need for heated dispensing lines.

    Handling Under Inert Atmosphere and Photosensitivity Considerations

    Storage at temperatures above −15 °C accelerates the liberation of elemental iodine through homolytic cleavage of the C–I bond. The vendor-recommended long-term storage condition is −20 ± 5 °C under a dry argon or nitrogen blanket, with the container shielded from UV and broad-spectrum visible light using amber borosilicate glass or secondary opaque overwrapping. Bulk shipments in 200 L PTFE-lined steel drums are blanketed with 0.2–0.3 bar(g) of argon and monitored for headspace oxygen content at each inventory reconciliation point. After the first inerted withdrawal, the headspace should be re-pressurized with argon to 0.1 bar(g); exposure to air for cumulative periods exceeding 15 min may introduce sufficient moisture and oxygen to initiate peroxy-iodine species formation, detectable by a darkening of the liquid beyond Gardner color 4. QC re-test data collected on retained samples indicate that assay loss remains below 0.5% absolute over 24 months when these conditions are maintained without interruption. For 1–5 kg laboratory-scale aliquots, transfer into septum-sealed amber vials and sparging with argon for 10 min prior to each use is sufficient to preserve coupling performance. Palladium-catalyzed carbon–carbon bond formation employing 5-iodo-2-methylthiazole as the limiting electrophile is widely documented in the construction of 2,5-disubstituted thiazole arrays for central nervous system (CNS) drug discovery programs. In a representative fragment-to-lead campaign, the compound was ligated to a 3-aminophenylboronic acid pinacol ester using PdCl2(dppf)·CH2Cl2 (1.2 mol%) and aqueous Na2CO3 in DME at 80 °C. Aqueous-organic phase separation followed by filtration through a 0.5 cm pad of Celite® and activated carbon reduced palladium bleed to <3 ppm, enabling direct telescoping into a subsequent Buchwald–Hartwig amination without intermediate chromatography. The iodine substituent does not participate in off-cycle hydrodehalogenation when thiol-based reducing agents such as dithiothreitol are present, a distinct advantage over the bromo analogue, which suffers 5–12% debromination under identical reductive amination conditions. Where the synthetic sequence requires differentiation of two halogen handles, 5-iodo-2-methylthiazole has been paired with 2-chloro-5-iodothiazole in a sequential Sonogashira–Suzuki protocol; the iodine para to the sulfur atom couples first at 25 °C with CuI (4 mol%) and Pd(PPh3)4 (2 mol%), leaving the 2-chloro site intact for a subsequent higher-temperature coupling.

    When Purity Specifications Exceed 99.5%: Applications in cGMP Manufacturing

    For active pharmaceutical ingredient (API) precursor synthesis under current Good Manufacturing Practice (cGMP), a minimum purity of 99.5% by HPLC (210 nm, C18 column, acetonitrile/water gradient) is often specified in the drug master file. The corresponding analytical release sheet includes a limits-of-elemental-impurities panel aligned with ICH Q3D: palladium must not exceed 10 ppm (USP <233>, ICP-MS), residual copper from elemental stabilizers is controlled below 15 ppm, and total non-volatile residue after combustion is <0.05%. The following table presents a typical cGMP-grade specification suite.
    ParameterLimitTest method
    Assay (HPLC, area%)≥99.5%In-house method TM-12I-001 (C18, UV 210 nm)
    Water content≤0.10%Ph.Eur. 2.5.12
    Palladium (Pd)≤10 ppmUSP <233>, ICP-MS
    Copper (Cu)≤15 ppmUSP <233>, ICP-MS
    Residual solvents (ethanol, THF)≤500 ppm eachUSP <467> (GC-HS)
    Appearance (25 °C)Clear, colorless to pale yellow liquidVisual inspection under D65 illumination
    Process-scale validation batches run in 2000 L glass-lined reactors (Pfaudler or equivalent) with double-mechanical seals and Hastelloy C-22 temperature sensor pockets have demonstrated lot-to-lot assay reproducibility within ±0.15% over fifteen consecutive campaigns. During pilot-plant execution, the exotherm associated with iodine–magnesium exchange for Grignard-type applications necessitates a jacket temperature ramp not exceeding 0.5 K·min−1 when the reaction mass exceeds 800 kg; deviation from this ramp rate has resulted in a temperature overshoot of 12–18 °C, triggering C–I bond homolysis and a corresponding 3–7% loss of active halide. When metalation is performed with i-PrMgCl·LiCl in THF at −30 °C, the iodine–magnesium exchange reaches >98% conversion within 20 min, monitored by quenched-flow GC aliquot analysis. The resulting magnesiated thiazole is stable for 4 h at −25 °C under rigorous inertion, after which the concentration of the active organometallic species decays at 1.2%·h−1 due to aggragative cluster formation identified by dynamic light scattering. Beyond small-molecule pharmaceuticals, 5-iodo-2-methylthiazole has been evaluated as a precursor to thiazole-2-methyl-functionalized ionic liquids for electrochemical double-layer capacitors. In this context, the residual halide content after metathesis must be driven below 50 ppm (IC, conductivity detector) to avoid parasitic faradaic reactions that reduce the operating voltage window below 2.7 V. The iodide is removed by sequential treatment with silver(I) tetrafluoroborate in acetonitrile, followed by passage through a 0.2 μm PTFE membrane filter; the process delivers a final bromide-plus-iodide sum below the 10 ppm detection limit of the method. Attempts to use the bromo analogue in the same sequence resulted in a persistent 200–400 ppm residual halide level and a 0.3 V contraction of the electrochemical stability window, reinforcing the operational advantage of the leaving-group lability of the iodo substitution when ultra-low halide thresholds are mandated by device performance requirements.