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HS Code |
780004 |
| Chemical Formula | C5H7NS |
| Molecular Weight | 113.18 |
| Appearance | Colorless to pale yellow liquid |
| Odor | Characteristic, pungent |
| Boiling Point | 155 - 156 °C |
| Melting Point | -21 °C |
| Density | 1.104 g/cm³ |
| Solubility In Water | Slightly soluble |
| Solubility In Organic Solvents | Soluble in common organic solvents |
| Flash Point | 46 °C |
| Refractive Index | 1.541 - 1.543 |
As an accredited 2,4-Dimethyl-1,3-Thiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 2,4 - Dimethyl - 1,3 - Thiazole in a sealed, labeled chemical - grade bottle. |
| Shipping | 2,4 - Dimethyl - 1,3 - Thiazole is shipped in well - sealed, corrosion - resistant containers. Shipment follows strict hazardous chemical regulations, ensuring proper handling, storage, and transportation to prevent leakage and ensure safety. |
| Storage | 2,4 - Dimethyl - 1,3 - Thiazole should be stored in a cool, dry, well - ventilated area. Keep it away from sources of ignition as it may be flammable. Store in a tightly closed container to prevent vapor release. Separate it from oxidizing agents and incompatible substances. Follow all safety regulations to ensure proper storage and prevent potential hazards. |
Thermal Generation of Roasted Notes in Extruded Snack SeasoningsThe incorporation of 2,4-dimethyl-1,3-thiazole into heat-processed savory flavor systems exploits its potent roasted, nutty, and meaty character, which develops further synergism when generated in situ alongside Maillard reaction intermediates. From a regulatory standpoint, its use as a flavoring substance is harmonized across major jurisdictions: it is listed under FEMA 3273, recognized as safe by the JECFA No. 1031 specification, and permitted within the European Union under Regulation (EC) No 1334/2008, where it appears in the Union List of flavouring substances with a purity requirement of not less than 98%. In a typical extrusion-coated snack seasoning powder, the active addition level of the thiazole ranges from 0.5 mg/kg to 5.0 mg/kg in the finished consumer product, with the concentrated seasoning blend containing between 0.05% and 0.5% by weight, diluted on a salt-and-maltodextrin carrier to facilitate uniform distribution during rotary drum adhesion. Manufacturing at scale frequently involves predispersion of the thiazole in a lipid-based or propylene glycol vehicle to mitigate the high vapor pressure that leads to evaporative losses of up to 35% when the liquid seasoning is held open-vat at ambient temperature prior to application. The downstream process centers on a continuous twin-screw extruder—a Wenger TX-57 or similar with an L/D ratio of 25:1—operating at a die temperature of 130–150°C and 14–18% moisture, after which the expanded collet is conveyed to a rotating cylindrical coating drum where atomized vegetable oil containing the premixed flavor solution is sprayed at a rate calibrated to achieve a final oil uptake of 6–8% on the base weight. A recognized production bottleneck emerges when the post-extrusion surface temperature of the collet exceeds 80°C at the spray nozzle interface: flash volatilization of the low-molecular-weight thiazole reduces retention efficiency below 60%, necessitating either a forced-air cooling step or the adoption of a sealed, recirculating vapour-capture hood to condensate and reintroduce escaped aroma compounds. The terminal products span puffed maize curls, extruded potato-based pellets, and directly expanded legume crisps, each presenting a differentiated matrix that influences the degree of aroma partitioning between the lipid coating and the carbohydrate bulk, an effect quantifiable through headspace gas chromatography monitoring of hexanal and thiazole peak area ratios over a 12-week shelf-life study at 40°C/75% RH.
What Role Does Encapsulation Efficiency Play in Bakery Fillings?Encapsulation of 2,4-dimethyl-1,3-thiazole into a glassy carbohydrate matrix becomes a critical unit operation when the raw dough enters a tunnel oven where air temperatures exceed 200°C and the core crumb temperature reaches 95–98°C for a dwell time of 12–18 minutes, conditions under which the free thiazole, with a boiling point of 144–145°C at atmospheric pressure, is driven off to an extent of 50–65% if unprotected. Regulatory compliance for bakery applications is established through FEMA 3273 and the JECFA No. 1031 purity monograph, and when marketed within the EU, the flavoring must further adhere to the positive-list designation under Regulation (EC) No 1334/2008 Annex I. The formulation addition ratio in the raw dough or un-baked filling typically ranges from 1 mg/kg to 10 mg/kg, but the exact loading is inversely correlated with the predicted thermal retention factor, which can be modeled by thermogravimetric analysis (TGA) performed at a ramp rate of 10°C/min under nitrogen flow. The industrial production workflow begins with spray-dry encapsulation using a tall-form dryer such as a Niro Atomizer with an inlet temperature set to 190 ± 5°C and an outlet temperature maintained at 95 ± 3°C, employing a wall material consisting of OSA-modified starch (Capsul® TA) and maltodextrin (DE 10–12) in a 3:1 ratio, into which the thiazole is pre-emulsified at a core load of 15–25% of the dry solids mass. The resulting free-flowing powder, with a mean particle size of 60–90 µm and a moisture content below 4%, is dry-blended into the flour component prior to the addition of water and fat, ensuring that the encapsulated oil droplets remain intact during the sheeting and moulding steps. A recurrent production anomaly noted on industrial laminating lines occurs when the encapsulated powder is subjected to high-pressure calendaring rolls operating with a gap clearance of less than 0.5 mm, which mechanically ruptures a fraction of the microcapsules and prematurely releases the volatile thiazole into the ambient plant atmosphere, causing a transient spike in airborne odor and a corresponding deficit in baked-in aroma that manifests as a flat, under-dosed character in the finished cracker or biscuit. Terminal product forms include fruit-preserve filled tarts, shelf-stable butter cookies consumed within 12-month expiry windows, and soft-crumb pound cakes where the encapsulation delays aroma release until the moment of mastication, thereby aligning the flavor perception with the texture breakdown rather than dissipating during storage.Extruded dry dog food kibble typically exhibits a bland cereal note after the high-temperature short-time (HTST) extrusion process; post-extrusion coating with a palatability enhancer containing 2,4-dimethyl-1,3-thiazole at 15–30 mg/kg in the fat-based coating significantly increases first-choice acceptance and consumption rate in two-bowl preference tests against a non-thiazole control, achieving an intake ratio exceeding 7:3 in standardized kennel panels. The pertinent regulatory pathway in North America is the GRAS notification for animal feed under FDA 21 CFR §582.60, augmented by the AAFCO Official Publication ingredient definitions, which classify synthetic flavoring substances identical to those approved for human food as acceptable feed additives, while in the EU, the substance may be introduced as a feed flavoring under Regulation (EC) No 1831/2003 provided it is registered within a premixture category. The addition level in the liquid coating emulsion is adjusted to deliver 10–20 mg/kg of thiazole in the finished pelleted ration, with the concentration verified by extraction into dichloromethane and quantification via GC-FID using an internal 2-isobutylthiazole standard, with a method detection limit of 0.1 mg/kg. The manufacturing sequence involves batch rendering of poultry fat or beef tallow to a peroxide value below 5 meq O₂/kg, cooling the fat to 48–52°C, and metering the thiazole along with sodium acid pyrophosphate and a mixed tocopherol antioxidant system under constant recirculation through a positive displacement pump into a vacuum coater—typically a Forberg or Lödige ploughshare mixer operated at a vessel pressure of −0.6 bar—where the fat aroma mixture is deposited onto the tumbling kibble mass at a ratio of 8–10% by weight. Oxidative degradation of the thiazole moiety in the presence of pro-oxidant transition metals such as iron and copper derived from meat meal ash presents a measurable stability risk: accelerated storage tests at 38°C/85% RH reveal a 40% reduction in thiazole concentration after 90 days when no chelating agent is employed, a loss rate that can be halved by the incorporation of citric acid at 0.2% of the fat phase. The finished products span adult maintenance dry diets in multi-wall paper bags with an inner polypropylene liner, semi-moist pouch-packed treats with a water activity of 0.60–0.65, and dental hygiene chews where the thiazole note masks the bitter off-taste of sodium hexametaphosphate added for tartar control.When 2,4-Dimethyl-1,3-Thiazole Serves as a Pivotal Building Block in Heterocyclic SynthesisDeploying 2,4-dimethyl-1,3-thiazole as an advanced intermediate for the construction of pharmacologically relevant scaffolds leverages the pronounced acidity of the C-5 proton, which facilitates regiospecific lithiation and subsequent functionalization to yield a library of 5-substituted-2,4-dimethylthiazoles employed in the discovery and scale-up of active pharmaceutical ingredients targeting metabolic and infectious disease pathways. Good Manufacturing Practice for such active pharmaceutical ingredient intermediates is governed by ICH Q7, and the chemical synthesis must occur within facilities compliant with ISO 9001:2015 quality management systems and, when destined for the European Economic Area, registered under REACH (EC) No 1907/2006 with a data dossier covering annual tonnage bands. The stoichiometric proportion of reagents in the key lithiation step requires a slight molar excess of 1.05 equivalents of n-butyllithium ( 2.5 M in hexanes) relative to the thiazole substrate to compensate for residual moisture in the tetrahydrofuran solvent system that has been pre-dried over a 3Å molecular sieve column to a water content below 50 ppm as verified by Karl Fischer titration. The downstream process at pilot scale is conducted in a 50 L glass-lined steel reactor equipped with a double mechanical seal and charged with anhydrous THF under a dry nitrogen atmosphere, cooled to −78 ± 3°C using a circulating bath of dry ice/acetone, and the n-BuLi is introduced via a jacketed dropping funnel at a rate that maintains the internal temperature below −65°C; after a 45-minute hold period to complete the deprotonation, the resulting lithiated thiazole is quenched with a large excess of crushed solid carbon dioxide, leading to the formation of 2,4-dimethylthiazole-5-carboxylic acid in yields routinely between 78% and 88% after acidification, extraction into ethyl acetate, and recrystallization from toluene/heptane (3:1). A critical process hazard identified during manufacturing campaigns arises from the exothermic nature of the n-BuLi quench and the potential for localized hot spots that can raise the temperature above −40°C, triggering premature ring-opening or polymerization; this is mitigated through the use of a magnetically coupled agitator delivering a tip speed of 1.2 m/s combined with an in-situ attenuated total reflectance (ATR) FTIR probe that tracks the disappearance of the thiazole C-5–H stretching vibration at 3125 cm⁻¹ in real time. The terminal output encompasses the 5-carboxylic acid derivative destined for amide coupling with piperazine derivatives under EDCI/HOBt activation to generate PPARγ partial agonists studied for type 2 diabetes, the 5-bromo derivative obtained via treatment with N-bromosuccinimide in DMF at 0°C which serves as a partner in palladium-catalyzed Suzuki-Miyaura cross-couplings, and the 5-acetyl derivative prepared through a Friedel-Crafts acylation protocol using acetyl chloride and aluminum trichloride in dichloromethane, employed as a precursor for chalcone synthesis in anti-infective research portfolios.
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| Property | 2,4-Dimethyl-1,3-thiazole | 2,5-Dimethyl-1,3-thiazole | 4-Methylthiazole |
|---|---|---|---|
| CAS No. | 541-58-2 | 1741-07-1 | 693-95-8 |
| Boiling point (°C) | 144–145 | 158–160 | 133–134 |
| Density (g·cm⁻³, 20 °C) | 1.019 | 1.036 | 1.093 |
| Refractive index n20/D | 1.5065 | 1.5140 | 1.5235 |
| FEMA GRAS No. | 3260 | 3316 | 3201 |
| JECFA No. | 1044 | 1031 | 1028 |
| EU Flavourings Reg. No. | 15.024 | 15.025 | 15.014 |
| Typical odor profile | Green, nutty, cocoa, vegetable | Roasted, meaty, sulfury, coffee | Green, tomato vine, alliaceous |