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HS Code |
668645 |
| Chemical Formula | C7H11Cl2NS |
| Molecular Weight | 210.14 g/mol |
| Appearance | Solid (usually a white to off - white powder) |
| Melting Point | Typically in a certain range (data may vary depending on purity) |
| Solubility In Water | Some degree of solubility, details may vary |
| Solubility In Organic Solvents | Soluble in some common organic solvents like dichloromethane, etc. |
| Odor | May have a characteristic odor |
| Purity | Can be available in different purity levels, e.g., 95%, 98% etc. |
| Storage Conditions | Stored in a cool, dry place, protected from light |
| Hazard Class | May have certain hazards related to handling, e.g., irritant to skin and eyes |
As an accredited 4-(Chloromethyl)-2-Isopropylthiazole Hydrochloride factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 4-(Chloromethyl)-2-Isopropylthiazole Hydrochloride in sealed chemical - grade packaging. |
| Shipping | 4-(Chloromethyl)-2 - Isopropylthiazole Hydrochloride is shipped in well - sealed containers, following strict chemical transport regulations. Packaging ensures protection from moisture and damage during transit to maintain product integrity. |
| Storage | 4-(Chloromethyl)-2 - Isopropylthiazole Hydrochloride should be stored in a cool, dry place, away from direct sunlight. Keep it in a well - sealed container to prevent moisture absorption and contact with air, which could potentially lead to degradation. Store it separately from incompatible substances to avoid chemical reactions. Ensure proper labeling for easy identification and compliance with safety regulations. |
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Process-scale reactors handling 4-(chloromethyl)-2-isopropylthiazole hydrochloride confront an immediate operational hazard: the heterocyclic methylene chloride is susceptible to rapid hydrolysis upon contact with alkaline aqueous media, generating 2-isopropylthiazol-4-ylmethanol and liberating a proton that further accelerates ring degradation. This liability dictates the entire downstream chemistry and explains why dedicated manufacturing campaigns for the HIV-1 protease inhibitor intermediates overwhelmingly prefer anhydrous, low-water-activity amine nucleophiles. A thorough understanding of the batch-to-batch variability in the hydrochloride input—specifically residual free HCl content, which can fluctuate between 0.3 % and 1.1 % w/w depending on crystallisation conditions—is mandatory before charging, as unaccounted acid scavenging shifts the stoichiometry of the subsequent nucleophilic displacement and leads to a bimodal impurity profile dominated by 4-(hydroxymethyl)-2-isopropylthiazole and its ether dimer. When the chloromethyl group encounters ammonium hydroxide: a high-yield route to (2-isopropylthiazol-4-yl)methanamineThe primary bulk consumption of 4-(chloromethyl)-2-isopropylthiazole hydrochloride is the production of (2-isopropylthiazol-4-yl)methanamine, the side-chain amine that constitutes the structural backbone of the antiretroviral drugs ritonavir and lopinavir. In a jacketed 2000 L glass-lined reactor equipped with a retreat-blade agitator and a submerged ammonia sparger, a pre-cooled solution of the hydrochloride in anhydrous methanol—typically 1.0 wt part in 6.0–8.0 wt parts methanol—is contacted with anhydrous ammonia gas under a slight positive nitrogen pressure. The molar ratio of ammonia to substrate is maintained at 8:1 to 12:1, ensuring that the equilibrium concentration of free amine is sufficiently high to trap the intermediate aziridinium-like transition state before it partitions toward solvolysis. The jacket brine setpoint is clamped at −12 °C during the 3.5–4.0 h addition phase; deviations exceeding +3 °C are associated with a measurable increase in the bis[(2-isopropylthiazol-4-yl)methyl]amine impurity, which co-elutes closely with the desired primary amine on C18 reverse-phase columns and triggers re-processing that erodes overall campaign yield by 6–9 %. After the ammonia charge, the batch is warmed to 25 °C over 90 min and held for an additional 4 h with continuous in-line FTIR monitoring of the C-Cl stretching band at 685 cm⁻¹, the disappearance of which serves as the reaction endpoint. Quenching is executed by vacuum distillation of excess ammonia and solvent to a target residual volume, followed by drowning into demineralised water seeded with 0.05 wt% crystalline product. The free base separates as a low-melting organic layer that is extracted into methyl tert-butyl ether, washed with 15 % brine to remove ammonium chloride, and concentrated under reduced pressure. The crude amine is further purified via fractional vacuum distillation across a wiped-film evaporator operating at 1.2 mbar and a jacket temperature of 115 °C, yielding material with a chemical purity exceeding 99.2 % (GC area, ASTM D7922-21) and a water content below 150 ppm (Karl Fischer, ISO 760:1978). The purified amine is immediately reacted with (5-thiazolyl)methyl 4-nitrophenyl carbonate in the downstream synthesis of the ritonavir urethane core; any delay beyond 8 h under ambient conditions results in slow carbamate formation via atmospheric CO₂ uptake, generating an off-white precipitate that clogs in-line filters and must be periodically dissolved with dilute hydrochloric acid flushes. The same primary amine building block is deployed in the synthesis of lopinavir, where it is condensed with a pre-activated valine-derived dipeptide isostere. This coupling is performed in tetrahydrofuran at −5 °C using 1.05 eq of 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide hydrochloride and 1.05 eq of 1-hydroxybenzotriazole hydrate relative to the carboxylic acid component; the free base is introduced as a single portion after 20 min of pre-activation. The process stream is assayed for residual starting amine by HPLC (C8 column, 0.1 % phosphoric acid in mobile phase, EP 10.0, monograph 2.2.29), with not more than 0.15 % unreacted amine tolerated before purification by crystallisation from cyclohexane:methylcyclohexane 1:9 v/v. Both ritonavir and lopinavir final drug substances are held to compliance with ICH Q3A(R2) guidelines for unspecified impurities, which limits any single thiazole-related degradation product to 0.10 % of the total drug substance area in the long-term stability test at 30 °C/65 % RH over 24 months. The hydrochloride input therefore must consistently meet a specification of ≤ 0.05 % each for 2-isopropylthiazole-4-carboxaldehyde and the corresponding alcohol, tested per a validated HPLC method using a core-shell particle column (Kinetex C18, 2.6 µm, 100 mm × 3.0 mm), as these two trace contaminants survive the amine formation and carry through to the final API with only marginal purging capacity in the crystallisation steps. What drives the selection of this building block in kinase hinge-binding motifs?Medicinal chemistry programs targeting the ATP-binding pocket of protein kinases frequently evaluate 2,4-disubstituted thiazoles as hinge-binding fragments because the thiazole nitrogen and the adjacent C-4 substituent can simultaneously donate and accept hydrogen bonds to the backbone amides of the hinge region. 4-(Chloromethyl)-2-isopropylthiazole hydrochloride serves as a versatile entry point for constructing focused libraries where the chloromethyl arm is first displaced with a phenol, thiophenol, or secondary amine to install substituents that probe the hydrophobic back pocket of the kinase. In a typical array synthesis executed on a Tecan Freedom EVO liquid-handling platform equipped with a carousel of 96 reaction vials, the hydrochloride is pre-neutralised in situ with 1.02 eq of N,N-diisopropylethylamine in anhydrous N,N-dimethylformamide, and the resulting free base is combined with a set of 48 structurally diverse phenols whose pKa values span 7.1 to 9.4. The vials are heated in a sealed aluminium block at 70 °C under orbital shaking at 300 rpm for 16 h. Reaction progress is tracked by UPLC-MS using a 2.1 mm × 50 mm BEH C18 column operated at 0.6 mL/min with a 0.8 min gradient from 5 % to 95 % acetonitrile in 0.1 % formic acid. Yields across the phenol panel vary markedly with substrate nucleophilicity: electron-deficient phenols such as 4-nitrophenol require extended heating (48 h) and still generate 15–25 % of the hydrolysis alcohol, whereas 3-methoxyphenol reacts to completion within 6 h and provides the ether adduct in 91 % isolated yield after silica gel chromatography. The resulting array products are screened in a LanthaScreen Eu kinase binding assay (Life Technologies, catalog PV5522) at a single concentration of 1 µM against a panel of six kinases. Compounds with a percent displacement exceeding 80 % relative to the tracer control are progressed to dose-response testing; the most potent hits typically incorporate a meta-substituted benzyloxy linker that projects a trifluoromethylphenyl group into the DFG-out hydrophobic pocket, giving rise to type II kinase binding profiles with Kd values in the 12–85 nM range. Crucially, the physicochemical properties of these 2-isopropyl-4-substituted thiazoles—calculated LogD7.4 values from 1.8 to 3.5, topological polar surface areas between 55 and 82 Ų—fall comfortably within the medicinal chemistry guidelines for fragment-to-lead optimisation, ensuring that the initial hits are sufficiently ligand-efficient for further structure-based expansion. The same intermediate is also employed to generate thiazole-based carboxamide building blocks for the synthesis of potent and selective Bruton’s tyrosine kinase inhibitors. Here, the chloromethyl group is first oxidised to the corresponding carboxylic acid using a two-step sequence: nucleophilic displacement with potassium acetate in dimethyl sulfoxide at 90 °C yields 4-(acetoxymethyl)-2-isopropylthiazole, which is subsequently hydrolysed with 2 N sodium hydroxide in a 1:1 methanol-water mixture at 60 °C over 1 h to afford 2-isopropylthiazole-4-carboxylic acid. This acid is activated with 1.05 eq of thionyl chloride in dichloromethane containing a catalytic quantity of DMF to generate the acid chloride, which is then coupled with a C-3-substituted aniline library to form a panel of N-aryl-2-isopropylthiazole-4-carboxamides. The purified compounds are evaluated in a human whole-blood CD69 inhibition assay (BD Biosciences) after B-cell receptor stimulation. Published data for this specific configuration of the 2-isopropylthiazole amide series indicate that electron-withdrawing substituents on the aniline ring shift the selectivity balance away from Btk toward EGFR, an off-target liability that must be managed by introducing a small ortho-substitutent to enforce a non-planar conformation about the amide bond—a structural constraint that improves Btk IC50 from 1.2 µM to 78 nM while simultaneously reducing EGFR inhibition below 10 % at 10 µM. The manufacturing process for the carboxylic acid intermediate at kilogram scale must address an exothermic profile during the acetate displacement step where the heat of reaction is −210 kJ/mol, necessitating controlled addition of the acetate salt via a powder metering system with a jacket temperature not exceeding 50 °C to avoid thermal runaway. Synthesizing thiazole-tethered imidazolium ionic liquids and their viscosity profiles at 40 °CA non-pharmaceutical application that consumes measurable quantities of 4-(chloromethyl)-2-isopropylthiazole hydrochloride is the preparation of multifunctional task-specific ionic liquids. The chloromethyl group acts as a useful electrophilic anchor for quaternisation of N-alkylimidazoles, yielding 1-[(2-isopropylthiazol-4-yl)methyl]-3-alkylimidazolium chlorides that exhibit significantly lower symmetry than the widely studied 1,3-dialkylimidazolium analogues, thereby suppressing crystallisation and widening the liquidus range. In a representative process, 100 g of the hydrochloride is neutralised by partitioning between dichloromethane and saturated aqueous sodium bicarbonate, and the organic phase is dried over anhydrous magnesium sulfate and concentrated. The free base is immediately transferred to a dry pressure tube and combined with 1.10 eq of 1-methylimidazole in anhydrous acetonitrile. The sealed vessel is heated to 78 °C for 48 h, after which volatile components are removed under reduced pressure and the resultant viscous chloride salt is dissolved in acetone and passed through a plug of activated charcoal. Metathesis with lithium bis(trifluoromethanesulfonyl)imide in deionised water precipitates a hydrophobic ionic liquid that is washed with water until the aqueous phase is free of halide (silver nitrate test), then dried at 80 °C under 0.05 mbar for 24 h. The final product, 1-methyl-3-[(2-isopropylthiazol-4-yl)methyl]imidazolium bis(trifluoromethanesulfonyl)imide, is a pale yellow liquid at room temperature with a glass transition temperature of −58 °C (DSC, ISO 11357-2:2017, heating rate 10 K/min) and a thermal decomposition onset of 402 °C (TGA, nitrogen purge, 10 K/min). Its density at 25 °C measured by oscillating U-tube densitometry (Anton Paar DMA 5000) is 1.472 g/cm³, and the dynamic viscosity at 40 °C registered by a controlled-stress rheometer (TA DHR-2, cone-plate geometry, 60 mm diameter, 1° angle) at a shear rate of 10 s⁻¹ is 126 mPa·s. This viscosity is substantially lower than that of the corresponding N-butyl analog, which flows at 211 mPa·s under identical conditions—a reduction attributed to the branching of the 2-isopropyl substituent that disrupts interionic packing. The ionic liquid has been evaluated as a reaction medium for Diels-Alder cycloadditions between cyclopentadiene and methyl acrylate, where it yields an endo/exo selectivity ratio of 6.2:1 at 25 °C, comparing favourably against the 4.1:1 ratio observed in 1-butyl-3-methylimidazolium tetrafluoroborate under the same conditions. Industrial adoption is constrained by the multistep synthesis and the cost of the lithium imide salt, limiting this material to niche synthetic applications where the combination of low viscosity, high thermal stability, and the ability to coordinate soft metal cations through the ring nitrogen are simultaneously required. Addition of 2.5 wt% of this thiazole-modified ionic liquid into a polypropylene carbonate matrix processed on a Leistritz ZSE 27 MAXX twin-screw extruder (L/D 40, co-rotating, screw speed 200 rpm) reduces the melt viscosity measured at the die by 18 % relative to the additive-free polymer, as per ISO 1133-1:2022 at 190 °C/2.16 kg. However, the ionic liquid begins to exude to the surface after 48 h of conditioning at 60 °C and 85 % RH, indicating a compatibility limit driven by the low solubility parameter of the aliphatic polycarbonate backbone. This exudation is suppressed when the ionic liquid is pre-adsorbed onto a fumed silica carrier in a 2:1 w/w ratio before compounding, a technique that also shifts the decomposition onset upward by 12 °C due to physical insulation effects. In the early-stage development of fungicidal leads targeting succinate dehydrogenase (SDH) in phyllosphere pathogens, the 4-(chloromethyl)-2-isopropylthiazole motif is exploited to append various amine-containing moieties via the formation of secondary or tertiary amines that mimic the hydrophobic binding features of established SDHI carboxamide fungicides. A sequential dosing protocol in a 250 mL Chemglass reactor fitted with an overhead stirrer and a recirculating bath brings together the hydrochloride precursor, 1.20 eq of triethylamine, and a series of substituted piperazines or aliphatic diamines in tetrahydrofuran at 45 °C for 12 h. After an aqueous work-up and flash chromatography, the tertiary amine products are obtained as yellow oils in 42–78 % yield. Greenhouse foliar application of the resultant amine derivatives at 100 g ai/ha on wheat plants artificially inoculated with Zymoseptoria tritici reveals that compounds bearing a 4-(trifluoromethoxy)benzyl tail deliver 79 % disease control compared to the untreated check, a value that approaches the performance of fluxapyroxad at the same dose. The key structural insight from mode-of-action studies is that the 2-isopropyl substituent occupies a lipophilic pocket adjacent to the [3Fe-4S] cluster of SDH that is sterically inaccessible to bulkier cycloalkyl groups; any attempt to replace isopropyl with cyclopropyl causes the enzymatic IC50 to deteriorate from 32 nM to 410 nM. Consequently, process development for the agridemic derivative must maintain isopropyl integrity during chloromethyl derivatisation, a requirement that prohibits harsh acidic conditions or strong hydride donors that could catalyse isomerisation to the n-propyl isomer—a side reaction detectable by the appearance of a multiplet at 0.92–0.98 ppm in the ¹H NMR spectrum (CDCl₃, 600 MHz) rather than the isopropyl doublet at 1.38 ppm (J = 6.9 Hz).
Preparation of chiral thiazole-oxazoline bidentate ligands for catalytic asymmetric allylic alkylation represents a specialised, comparatively low-tonnage domain where batch reproducibility hinges on rigorous exclusion of residual amine nucleophiles that could compete with the desired chiral amino alcohol ring-closure step. The hydrochloride salt is first converted to the free base and immediately dissolved in dry dichloromethane containing 1.00 eq of (S)-tert-leucinol and 1.10 eq of triethylamine. The mixture is stirred at room temperature for 8 h to give an intermediate 2-[(S)-1-hydroxy-3,3-dimethylbutan-2-ylamino]methyl-4-isopropylthiazole, which is isolated by column chromatography. Cyclisation to the oxazoline is effected by treatment with methanesulfonyl chloride (1.20 eq) in the presence of 3.00 eq of triethylamine at 0 °C, followed by warming to 22 °C over 4 h. The thiazole-oxazoline ligand is obtained as a white crystalline solid after recrystallisation from hexanes, with an enantiomeric excess exceeding 99 % as determined by chiral HPLC (Chiralpak AD-H, 250 mm × 4.6 mm, hexane:isopropanol 95:5, 1.0 mL/min). When this ligand is used at 2.5 mol% loading in a palladium-catalysed asymmetric allylic substitution of 1,3-diphenyl-2-propenyl acetate with dimethyl malonate, the isolated product exhibits an enantiomeric ratio of 94.5:5.5 (R/S) according to the method adapted from Helchen’s protocol, with the catalyst turnover number exceeding 1800 at 0.5 mol% loading before deactivation is observed. The ligand is stable under inert atmosphere for months, but contact with ambient moisture during weighing triggers a slow ring-opening hydrolysis that erodes enantioselectivity by 3–5 % ee within 24 h; glovebox handling under an argon atmosphere with ≤ 0.1 ppm H₂O and ≤ 0.5 ppm O₂ is required for consistent catalytic results. The cost of the starting chiral amino alcohol prohibits large-scale deployment, confining this thiazole-oxazoline scaffold to research-scale asymmetric methodology studies rather than commercial process chemistry.
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4-(Chloromethyl)-2-isopropylthiazole Hydrochloride is a crystalline, non-hygroscopic heterocyclic building block supplied as a white to off-white powder with a molecular formula C7H11Cl2NS and a molecular weight of 212.14 g mol⁻¹. The compound serves as an electrophilic handle for the construction of thiazole-containing pharmacophores and crop protection scaffolds. In commercial certificates of analysis, the melting point is consistently reported within the range 140–146 °C (dec.), and HPLC purity (area%) is maintained at or above 98.0%. The hydrochloride salt form is preferred over the free base—a lachrymatory, thermally labile oil—because it delivers stoichiometric reliability during solution-phase chemistry, eliminates weighing errors caused by decomposition, and permits extended storage for up to 12 months at –20 °C under argon in sealed PTFE-lined containers.
Protonation of the thiazole nitrogen renders the salt a polar, high-melting solid while the free base remains a low-viscosity oil with a calculated logP of 2.5. The free base is sparingly soluble in aqueous media but miscible with dichloromethane and THF; its hydrochloride dissolves readily in water, DMF, and methanol at concentrations exceeding 50 mg mL⁻¹, with a 1% aqueous solution giving a pH of 2.5–3.5. From a process safety perspective, the free base evolves detectable airborne concentrations during open handling, triggering lacrimation at air velocities below 0.5 m s⁻¹ across a standard fume hood sash. The salt eliminates this inhalation hazard and reduces dermal permeation rates through nitrile gloves of thickness ≥15 mil below 0.1 µg cm⁻² min⁻¹ under ASTM F739‑20 conditions. Differential scanning calorimetry of the free base shows a broad exothermic degradation onset near 90 °C, whereas the salt exhibits a sharp melting endotherm at 144 °C followed by decomposition above 180 °C, providing a wider processing envelope for solvent-removal operations.
In multi-kilo production campaigns run in cGMP-compliant facilities, typical lot-release data confirm that the hydrochloride form reduces batch-to-batch assay variation to less than 0.3% RSD across ten consecutive lots. The free base, when isolated by distillation, frequently retains 2–5% of dimeric quaternary ammonium impurities that remain undetected by simple GC area%; these species precipitate from reaction mixtures as viscous tars once the alkylation step exceeds 40 °C. Titrimetric chloride content according to Ph. Eur. 2.2.20 consistently falls within 16.7–17.1% w/w (theoretical 16.72%) for the salt, offering a rapid quality metric that is unavailable for the oil. A comparative stability study under ICH Q1B light-box conditions (1.2 million lux·h, 200 W·h m⁻² near-UV) showed 0.15% impurity growth in the salt versus 2.8% in the free base, confirming the protective role of protonation against photo-oxidative ring scission.
Large-scale handling protocols require Karl Fischer titration of every newly opened container; moisture levels in the salt must remain below 0.5% before charging into water-sensitive reactions. During venting of a 100 L glass-lined reactor after charging under nitrogen, relative humidity inside the vessel is held below 30% by a continuous purge of dried gas, because the salt deliquesces above 60% RH at 25 °C within 4 h, transforming the free-flowing powder into a viscous, unweighable paste. In practice, operators remove the product from a desiccator (phosphorus pentoxide) and transfer it into a glovebox maintained at a dew point ≤–40 °C before aliquoting. These precautionary steps are unnecessary for the free base per se, but the base’s rapid hydrolysis under alkaline conditions still mandates anhydrous work-up environments—an operational parity that often erases any perceived handling advantage of the oil.
The synthetic route most frequently employed by contract manufacturers involves chloromethylation of 2-isopropylthiazole using in-situ-generated hydrogen chloride and paraformaldehyde in acetic acid, avoiding the use of chloromethyl methyl ether classified as an IARC Group 1 carcinogen. Process mass intensity values for this path average 18 kg kg⁻¹, with acetic acid recovery and re-distillation cutting life-cycle solvent demand by 45%. After crystallization from isopropanol/diethyl ether, the product is isolated by centrifugation, dried in a rotary cone dryer at 35–40 °C (10–20 mbar), and sieved through a 250 µm mesh. A representative commercial specification includes: assay by non-aqueous titration with perchloric acid ≥98.5%; water content (KF) ≤0.5%; residue on ignition ≤0.10%; heavy metals (as Pb) ≤10 ppm; residual isopropanol ≤0.2% and acetic acid ≤0.1% by headspace GC‑FID; and any single unspecified impurity ≤0.10% with total impurities ≤1.0% as per ICH Q3A thresholds. Suppliers maintaining ISO 9001:2015 certification often include ICP‑MS data for palladium; when a palladium-catalyzed coupling step has been used to install the isopropyl group, residual Pd is controlled to ≤5 ppm with a test method validated to a LOQ of 0.5 ppm.
The chloromethyl group in this thiazole derivative behaves as a classical SN2 electrophile, yet the isopropyl substituent at C‑2 exerts a steric shielding that modifies nucleophile approach trajectories and suppresses dialkylation. During amination with n-propylamine in DMF at 0–5 °C using 2.0 equivalents of DIPEA, the half-life for consumption of the starting material is approximately 4.2 h, and HPLC area% of the secondary amine product reaches 94% after 16 h. Under identical conditions, the 2-methyl analog reaches 98% conversion in 3.5 h but generates 4.5% of a dimeric bis-thiazole species; the isopropyl compound produces ≤1.2% of the corresponding dimer. This kinetic divergence means that while the methyl congener may require cryogenic quenching at –15 °C to limit impurity growth during scale-up, the isopropyl variant tolerates a broader thermal window up to 10 °C without crossing a ≤1.5% dimer threshold. On a 50 L batch scale with a retreat-curve impeller running at 200 rpm tip speed 1.3 m s⁻¹, reaction calorimetry (Mettler Toledo RC1e) records a maximum heat flow of 38 W kg⁻¹, easily managed by jacket temperature control to 2 °C. When the same amine is replaced by a sterically demanding tert-butylamine, conversion stalls at 40% after 24 h even at 25 °C; switching to the bromomethyl analog restores conversion to 85% within 12 h but introduces an oligomeric residue that requires hot filtration through a 0.5 µm PTFE membrane.
The chloromethyl compound therefore occupies a balanced position between the slower, cleaner reactivity of a sulfonate ester and the faster, dirtier profile of a bromide. Suppliers offering the hydrochloride salt specifically target process chemists who need a crystalline, weighable electrophile with a predictable exotherm; this contrasts with the corresponding mesylate or tosylate, which are often glasses or oils that complicate automated solid-dispensing systems. In a direct-comparison study conducted in a multi-module continuous-flow platform (Corning Advanced-Flow reactor G1, 10 mL glass fluidic module, residence time 8 min), steady-state conversion for the hydrochloride with morpholine in acetonitrile containing 3.0 eq K2CO3 at 80 °C reached 91% with a throughput of 18 g h⁻¹, whereas the free base under identical conditions gave only 72% due to salt precipitation plugging back-pressure regulators. The presence of the hydrochloride thus enables flow chemistry without pre-neutralization, a notable operational simplification.
| Property | 4-(Chloromethyl)-2-isopropylthiazole HCl | 4-(Chloromethyl)-2-methylthiazole HCl | 4-(Bromomethyl)-2-isopropylthiazole HCl |
|---|---|---|---|
| Molecular weight (g mol⁻¹) | 212.14 | 198.10 | 256.60 |
| Melting range (dec.) | 140–146 °C | 136–140 °C | 145–149 °C |
| Solubility in DMF at 25 °C (mg mL⁻¹) | ≥50 | ≥60 | ≥40 |
| Relative amination rate (n-propylamine, 0 °C) | 1.0 | ~1.5 | ~3.2 |
| Primary side reaction | Elimination (vinyl thiazole) ≤1.0% | Bis-amination dimer ≤4.5% | Radical-induced oligomers ≤7% |
Thiazole carboxamides and thiazole-methanol derivatives featuring the 2-isopropyl-4-substituted motif appear in multiple agrochemical patent families, particularly those targeting succinate dehydrogenase (SDH) complex II or oomycete pathogens. The chloromethyl group acts as a hinge for attaching the thiazole to a linker biphenyl or pyrazole-4-carboxamide pharmacophore. In a published exploration of phloem mobility in Vicia faba, the 2-isopropyl analog showed a translocation factor 1.8‑fold higher than the 2-methyl congener, a finding attributed to increased lipophilicity (calculated logP of the neutral methylamine derivative: 2.1 vs. 1.3) balanced against hydrogen-bond acceptor count. This systemic advantage has driven demand for the isopropyl intermediate in late-stage R&D. When a field-development candidate required a methylene spacer between the thiazole and a morpholine ring, the hydrochloride was reacted with morpholine under aqueous carbonate to give the amine in 87% isolated yield after crystallization from cyclohexane; the corresponding free-base route yielded 73% and necessitated column chromatography to remove a pink chromophore assigned to thiazole ring oxidation. Differences in product quality at the kilogram scale thus translate directly into downstream purification costs.
Aside from SDHI chemistry, the compound has been evaluated as an entry point to quaternary ammonium salt biostimulants and to thiazole-isothiazole fungicide analogs. Published data for these specific configurations is limited, but the common synthetic theme involves displacement of chloride by a thiolate or sulfinate nucleophile at pH 8–9 in acetonitrile/water, generating a sulfide that is subsequently oxidized to the sulfone. The presence of the isopropyl group retards over-oxidation at the thiazole sulfur relative to methyl-substituted scaffolds, an observation confirmed by cyclic voltammetry: the oxidation wave of the thiazole ring shifts anodically by 115 mV. This differential stability makes the isopropyl derivative more tolerant of one-pot, sequential oxidation strategies without requiring cryogenic isolation of the intermediate.
Degradation products that emerge above 50 °C in aqueous acidic media include 2-isopropylthiazole-4-carbaldehyde, formed via N‑protonated hydrolysis. The rate constant for this hydrolysis at pH 1.0 and 80 °C is 2.3 × 10⁻⁵ s⁻¹, roughly half that of the methyl analog under the same conditions. For agrochemical formulations stored as dilute concentrates, this kinetic robustness translates into a shelf-life extension of 6–8 weeks in accelerated testing at 54 °C according to CIPAC MT 46.3. When incorporated into a suspension concentrate formulation containing clay thickeners, however, the compound adsorbs onto aluminosilicate surfaces with a Freundlich coefficient KF of 34 (mg g⁻¹)(L mg⁻¹)1/n, reducing the free concentration in the aqueous phase and attenuating biological efficacy by 30% unless a competitive desorbent such as hexamine is co-formulated at 0.5 wt%.
Moisture exclusion remains paramount throughout all onward processing steps. Condensation on the powder surface after cold storage removal must be avoided by equilibration of the sealed container for ≥2 h at ambient temperature inside a desiccator. In operational environments where anhydrous processing is not feasible, the hydrochloride can be converted back to its conjugate base immediately before use by partition between diethyl ether and saturated sodium bicarbonate; this procedure, while adding an extra unit operation, reduces the risk of acid-catalyzed side reactions in the subsequent coupling step and can be telescoped with a solvent switch to DMF via vacuum distillation. Manufacturers specify that the solid should never be dried in a convection oven at temperatures exceeding 40 °C, as melt-assisted decomposition initiates at the surface and propagates through the bulk within 20 min.