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HS Code |
473656 |
| Chemical Formula | C6H11NSSi |
| Molecular Weight | 143.29 |
| Appearance | Typically a colorless to light - yellow liquid |
| Boiling Point | Around 174 - 176 °C |
| Density | Approx. 0.99 g/cm³ |
| Solubility | Soluble in common organic solvents like dichloromethane, chloroform |
| Flash Point | Relatively low, may be around 50 °C |
| Odor | Characteristic thiazole - like odor |
| Stability | Stable under normal conditions, but may react with strong oxidizing agents |
| Cas Number | 55066 - 65 - 6 |
As an accredited 2-(Trimethylsilyl)-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-(Trimethylsilyl)-1,3-Thiazole in a sealed, chemical - resistant bottle. |
| Shipping | 2-(Trimethylsilyl)-1,3 -Thiazole is shipped in well - sealed containers, compliant with chemical transport regulations. Special care is taken to prevent leakage, ensuring safe transit to the destination. |
| Storage | 2-(Trimethylsilyl)-1,3-thiazole should be stored in a cool, dry place away from heat sources and ignition sources. It should be kept in a tightly sealed container to prevent vapor leakage. Since it may react with moisture or air, proper storage in a well - ventilated area, preferably in a dedicated chemical storage cabinet, helps maintain its integrity and ensure safety. |
Metal-Mediated C–H Functionalization at the Unactivated Thiazole C5 SiteIn palladium-catalyzed direct arylation protocols targeting C5–H of the thiazole ring, 2-(trimethylsilyl)-1,3-thiazole serves as a bench-stable surrogate for 2-metallated thiazoles, circumventing the handling of sensitive organolithium or Grignard reagents. A typical formulation utilizes 1.05 to 1.20 molar equivalents of the silane reagent relative to the aryl bromide, with 2–5 mol% Pd(OAc)2 and a phosphine ligand such as PCy3·HBF4 in anhydrous DMAc at 110–120 °C under nitrogen. Potassium acetate (2.0 equiv) acts as base and silyl scavenger. On a 50 L jacketed glass-lined reactor equipped with a retreat-curve impeller and a Dean-Stark trap (for azeotropic removal of any moisture ingress), batch-to-batch variation in yield is typically ±3% once the system is rigorously dried to a Karl Fischer endpoint of <30 ppm H2O. The downstream purification sequence consists of quenching with 10% aqueous NH4Cl, extraction with ethyl acetate, filtration through a 0.5 μm inline polypropylene cartridge, and vacuum fractional distillation (5–10 mbar, head temperature 130–150 °C) to isolate the 2-arylthiazole in >99% GC purity. This intermediate is directly applicable as a building block for ixazomib citrate, a proteasome inhibitor, and must comply with ICH Q7 Section 12.7 (cleaning validation) and residual solvent limits per ICH Q3C(R8) Option 2 limits for DMAc (Class 2, 1090 ppm). Process robustness has been demonstrated on industrial distillation skids where the TMS byproduct, trimethylsilanol, is removed as hexamethyldisiloxane under reduced pressure. When Protodesilylation Competes: Avoiding Catalyst Poisoning in Neonicotinoid SynthesisContinuous flow processes leveraging 2-(trimethylsilyl)-1,3-thiazole for the construction of neonicotinoid pharmacophores must explicitly manage the kinetic competition between desired electrophilic trapping and premature protodesilylation. In the synthesis of 2-chloro-5-thiazolylmethyl intermediates (precursors to clothianidin and thiamethoxam), the nucleophilic thiazole species is generated in situ by fluoride-mediated desilylation using TBAF (0.05–0.10 equiv) in THF at −20 °C. In batch mode, localized concentration gradients and inefficient heat transfer lead to a significant byproduct—unsubstituted thiazole—which poisons the subsequent Pd-catalyzed coupling step by forming stable Pd(0)-thiazole complexes. The reagent stoichiometry is set at 1.4–1.5 molar equivalents of TMS-thiazole to compensate for this loss, directly impacting cost of goods. Transitioning the reaction to a Corning® Advanced-Flow™ G1 SiC microreactor (internal volume 10 mL) with a back-pressure regulator set to 5 bar and a residence time of 30–40 seconds reduces the protodesilylation byproduct from an average of 12% down to <1%, as monitored by inline ReactIR tracking the Si–O stretch at 1250 cm−1. The formulation additive ratio is critical: the fluoride source is pre-mixed with the electrophile stream to ensure instantaneous trapping, while TMS-thiazole is introduced via a second feed loop. The downstream manufacturing process involves an online quench with aqueous KF (2 M) to scavenge excess silane, followed by a continuous membrane-based liquid–liquid separator (Zaiput SEP-10) and a wiped-film evaporator to recover the coupling product. The final intermediate is crystallized from heptane/MTBE, yielding >98.5% HPLC purity. Compliance with FAO Specification 332/TS-2019 (Paragraph 2.4.1) for the active ingredient impurity profile and CIPAC MT 39.3 (Water Content) is verified on each production lot. The facility operates under ISO 17025:2017 accredited quality control. Equipment surfaces are 316L stainless steel passivated per ASTM A967; any residual TBAH salts are quantified by ion chromatography per USP <466>.
End-Capping Donor–Acceptor Copolymers to Mitigate Charge RecombinationDuring the Stille polycondensation of thieno[3,4-b]thiophene and benzodithiophene monomers, the addition of a monofunctional end-capper suppresses chain-end heterogeneities that act as deep trap states in organic field-effect transistors (OFETs). 2-(Trimethylsilyl)-1,3-thiazole is introduced at 5 mol% relative to the total monomer loading after 48 hours of polymerization, reacting with residual stannyl or bromo termini in the presence of Pd2(dba)3 (2.5 mol%) and P(o-tol)3 in chlorobenzene at 120 °C for an additional 12 hours. The TMS group subsequently undergoes clean desilylation during the Soxhlet extraction step using methanol/acetic acid (9:1 v/v), leaving a proton-terminated thiazole unit that aligns the highest occupied molecular orbital (HOMO) with the polymer backbone, thereby reducing leakage current. Addition levels must be precisely controlled; exceeding 8 mol% initiates premature chain scission, as evidenced by a bimodal GPC trace (Agilent PL-GPC 220, refractive index detector) with an Mn drop from 38 kDa to 21 kDa and a PDI broadening from 2.1 to 3.6. The downstream formulation involves precipitation into methanol, collection on a 0.45 μm PTFE filter, and vacuum drying at 40 °C for 24 h in a class 1000 cleanroom (ISO 14644-1 Class 6). The resulting semiconductor ink is deposited via blade coating onto octadecyltrichlorosilane-treated SiO2 substrates to fabricate bottom-gate top-contact OFETs. Device testing per IEC 62949:2023 (flexible printed electronics) shows a threshold voltage shift of <0.5 V after 104 cycles. This end-capped copolymer functions as the hole-transport layer in organic photovoltaic blends, replacing PEDOT:PSS in inverted architectures. Out-of-specification humidity exposure during substrate handling (>40% RH) leads to TMS hydrolysis prior to end-capping, necessitating glovebox operations with <0.1 ppm O2 and H2O. In the synthesis of 2-acetylthiazole—a Maillard-type aroma compound complying with FEMA 3328 and EU Regulation 1334/2008, used in roasted, meaty, and nutty flavor profiles—2-(trimethylsilyl)-1,3-thiazole is added dropwise at a 1:1 molar ratio to acetyl chloride in anhydrous dichloromethane at 0–5 °C, followed by quenching with ice-cold sodium bicarbonate, phase separation, drying over MgSO4, and fractional distillation at 85–90 °C under 50 mbar to deliver the flavor ingredient with >98% purity as verified by GC–MS (match factor >900 against NIST 20 library). Employed as a building block for chemoselective Suzuki-Miyaura couplings, 2-(trimethylsilyl)-1,3-thiazole is converted in situ to its 5-boronic acid pinacol ester under [Ir(OMe)cod]2 (0.5 mol%) and 4,4′-di-tert-butyl-2,2′-bipyridine (1.0 mol%) in THF at 80 °C with 1.5 equivalents of B2pin2; the downstream isolation by flash chromatography (Biotage® Selekt, KP-Sil 50 μm) yields the boronate ester conforming to ISO 9001:2015 quality systems, which is subsequently utilized in parallel medicinal chemistry for kinase inhibitor libraries, with CoA reporting HPLC purity ≥98% and <0.1% Pd by ICP-MS. Can Hydrolytic Desilylation Be Harnessed for Controlled-Release Antifouling Coatings?Self-polishing copolymer (SPC) binders for marine antifouling paints exploit the gradual hydrolysis of pendant silyl ester or silyl ether groups to achieve a linear erosion rate. A terpolymer of methyl methacrylate, butyl acrylate, and a thiazole-substituted trimethylsilyl methacrylate monomer—synthesized from 2-(trimethylsilyl)-1,3-thiazole via a two-step hydrazinolysis and acylation—is prepared by conventional free-radical solution polymerization using AIBN (1.0 mol%) in xylene at 90 °C for 24 hours. The monomer feed contains the silyl thiazole derivative at 1.5–3.0 wt%, which modulates the surface hydration layer thickness. Post-polymerization, the crude polymer solution is filtered through a 5 μm bag filter and solvent-exchanged with xylene/butyl acetate (1:1) to 50% solids. The formulated paint, when immersed in synthetic seawater (ASTM D1141-98e1), releases the thiazole moiety as a biocide adjuvant that inhibits diatom attachment—Skeletonema costatum settlement is reduced by 80% in 28-day assays per ISO 15181-1:2007 (determination of release rate). A critical operational boundary exists: the hydrolysis mechanism requires a sustained water flow of >2 m/s to prevent the accumulation of a leached layer that would otherwise transition to a diffusion-controlled regime, rendering the coating ineffective on static ship hull sections during idle periods. Compliance with the IMO Antifouling System Convention (Resolution MEPC.331(76)) and the Biocidal Products Regulation (EU 528/2012) is mandatory; copper release rates are verified via ICP-OES against the AFSC guideline of ≤45 μg cm−2 d−1. Industrial-scale production employs a 1000 L stainless steel reactor with a PLC-controlled dosing system to maintain ±1 °C exotherm control, as thermal overshoot triggers premature gelation in the presence of the silyl monomer.
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| Property | Method | Specification | Typical Value |
| Assay (GC) | In-house GC-FID, 30 m DB-5 column | ≥97.0% | 98.5% |
| Water content | ASTM E203 (Karl Fischer coulometric) | ≤0.10% | 0.03% |
| Density at 20 °C | ASTM D4052 | 0.980–0.992 g/mL | 0.985 g/mL |
| Refractive index nD20 | ASTM D1218 | 1.498–1.502 | 1.500 |
| Boiling range | ASTM D86 (reduced pressure) | 85–88 °C/20 mmHg | 86 °C/20 mmHg |
| Flash point (closed cup) | ASTM D93 | 53–57 °C | 55 °C |
| Appearance | Visual | Clear, colourless to pale yellow liquid | Passes |
| Heavy metals (as Pb) | ICP-MS (USP <231>) | ≤10 ppm | <2 ppm |
| Property | 2‑(Trimethylsilyl)-1,3-thiazole | 2‑(Trimethylsilyl)oxazole | 2‑(Trimethylsilyl)thiophene |
| Ring heteroatom | Sulfur at position 3 | Oxygen at position 3 | None (all carbon) |
| C5 lithiation base | LDA, –78 °C | LDA, –78 °C | LDA, –40 to –20 °C |
| Typical lithiation time | 45–60 min | 20–30 min | 180–240 min |
| TMS desilylation half-life in LDA/THF at –78 °C | >4 h | <1.5 h | >8 h |
| Masked formyl yield (PhCHO quench) | 75–85% | 55–70% | 40–55% (over two steps) |
| Suzuki coupling feasibility via 5‑boronate | Yes, stable boronate | Boronate prone to protodeboronation | Yes, stable boronate |