|
HS Code |
902912 |
| Chemical Formula | C8H6N2S2 |
| Molar Mass | 194.28 g/mol |
| Solubility In Water | Low solubility (due to non - polar nature of the thiazole and pyridine rings) |
| Solubility In Organic Solvents | Soluble in common organic solvents like dichloromethane, chloroform (due to non - polar character) |
| Pka | No common pKa value found (acid - base properties would depend on protonation of nitrogen atoms in rings) |
| Stability | Stable under normal conditions, but may react with strong oxidizing or reducing agents |
As an accredited 4-(Pyridin-4-Yl)-1,3-Thiazole-2(3H)-Thione factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 4-(Pyridin - 4 - yl)-1,3 - thiazole - 2(3H)-thione in sealed chemical - grade packaging. |
| Shipping | 4-(Pyridin - 4 - yl)-1,3 - thiazole - 2(3H)-thione is a chemical. Shipping must comply with relevant hazardous material regulations. It should be properly packaged to prevent leakage during transit. |
| Storage | Store 4-(Pyridin-4-yl)-1,3-thiazole-2(3H)-thione in a cool, dry place, away from heat sources and direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and exposure to air, which could potentially lead to degradation. Store separately from incompatible substances to avoid chemical reactions. |
What Dictates Scorch Safety in High-Speed Passenger Tire Production?In compounding of diene elastomers for radial tires, accelerator systems based on sulfenamide derivatives typically deliver an adequate balance between cure rate and processing security, yet the risk of premature crosslinking during high-temperature extrusion—especially on pin-barrel cold-feed extruders with L/D ratios exceeding 16:1—demands a supplementary scorch inhibitor that does not plateau at the prevailing stock temperature of 105–115 °C. 4-(Pyridin-4-Yl)-1,3-Thiazole-2(3H)-Thione operates as a pre-vulcanization retarder through reversible coordination with soluble zinc complexes present in the compound, raising the threshold temperature for incipient gel formation by approximately 8–12 °C when dosed at 0.15–0.40 phr. The material is integrated downstream of carbon black incorporation on an intermeshing tangential internal mixer (typical batch weight 180–250 kg) with drop-door temperature set no higher than 120 °C to avoid irreversible disaggregation of the thione tautomer. Dynamic cure kinetics measured by a moving-die rheometer per ASTM D5289 show an elongation of the ts2 parameter by 25–40 % relative to an unprotected control, while the t90 plateau cure time rises by less than 8 %, preserving factory throughput in multi-cavity steam presses. Regulatory requirements for rubber articles destined for food-contact applications invoke FDA 21 CFR § 177.2600 and BfR Recommendation XXI, and extractives must remain below 0.1 mg/dm² in aqueous simulants. Finished goods encompass passenger-car tire inner liners, engine mount bushings subjected to 2.5–3.0 G dynamic stiffness, and extruded weather-seal profiles where a Mooney viscosity ML(1+4) at 100 °C of 45–60 MU must be maintained for dimensional stability. In matrix-acidizing treatments for carbonate reservoirs, a high-strength hydrochloric acid blend (15–28 % wt) is pumped under pressure to create wormhole channels, yet the extreme corrosivity toward coiled-tubing steel grades such as CT 90 and HS-80 necessitates the addition of a filming-inhibitor package stable at bottom-hole temperatures that can exceed 130 °C in the Ghawar or Permian Basin formations. 4-(Pyridin-4-Yl)-1,3-Thiazole-2(3H)-Thione provides a strong multidentate adsorption onto ferritic-pearlitic surfaces through the endocyclic sulfur atom and the pyridyl nitrogen lone pair, with laboratory autoclave tests conducted according to NACE TM0198-2021 demonstrating a corrosion rate reduction from 45 mm/y to below 5 mm/y at a concentration of 0.5–2.0 vol % of the total acidizing fluid. The inhibitor is pre-dissolved in a glycolic or methanol-based carrier before being metered into the blender tub of a skid-mounted acid-pumping unit operating at up to 15 bbl/min. Compatibility with mutual solvents such as ethylene glycol monobutyl ether must be verified through a jar-test protocol defined by API RP 42, as phase separation would lead to uneven filming on the downhole tubulars. Discharged post-flowbacks are assessed per OSPAR Commission Guideline 2005/2 for ecotoxicological persistence, and the product’s log Kow below 2.8 indicates a limited bioaccumulation risk in produced-water discharges. The terminal application remains a stimulation campaign in a sour-gas producer, where the treated interval extends from 3 200 m to 4 100 m measured depth, targeted at a matrix permeability enhancement from single-digit milliDarcies to an expected 30–50 mD post-acidization. Operating a Non-oxidizing Biocide Program Under Elevated pH and Biofilm StressOpen recirculating cooling-water loops that run on high-alkalinity makeup water often settle at a bulk pH of 8.6–9.2, a regime where conventional isothiazolinone chemistries undergo ring-opening hydrolysis at a half-life below 48 h at 35 °C, driving operators to increase slug-feed frequency or alternate with glutaraldehyde-based blends. 4-(Pyridin-4-Yl)-1,3-Thiazole-2(3H)-Thione exhibits a hydrolytic-stability window that extends effective half-life beyond 120 h at pH 9.0, owing to the electron-withdrawing pyridinium mesomerism that shields the thioamide linkage. An active-ingredient residual of 5–25 mg/L, determined by HPLC-UV with a C18 column validated under ISO 16266 protocols for Pseudomonas aeruginosa, is maintained via proportional-dosing pumps triggered by an online oxidation-reduction potential set point of 350–450 mV versus Ag/AgCl. The program is assessed quarterly through sessile-bacteria swab kits conforming to ASTM D8075, and total planktonic counts must stay below 10⁴ CFU/mL to satisfy the risk-management thresholds published in ASHRAE Standard 188-2021 for Legionella control. In systems where the cooling tower basin receives wind-blown dust with elevated iron content, a supplemental chelating dispersant at 2–5 mg/L active is required to prevent extracellular polymeric substance stabilization, a scenario observed repeatedly in Middle Eastern petrochemical complexes. The end-use context is a 12 000 m³/h circulating-water installation serving a mixed-feed cracker, and the discharged blowdown must meet the local consent-limit for total organic halogens (AOX < 0.1 mg/L), verified through pyrolysis-microcoulometry per DIN EN 1485. A class of sulfur-bearing heterocycles functions as levelers and grain refiners in acid-copper electroplating baths used for through-hole metallization in printed-circuit boards, where deposit uniformity across a 1:20 aspect-ratio via is governed by the suppression of protrusion growth on high-current-density surface regions. 4-(Pyridin-4-Yl)-1,3-Thiazole-2(3H)-Thione, added to a virgin-makeup solution containing 200–220 g/L CuSO₄·5H₂O and 50–65 g/L H₂SO₄ at a concentration of 5–20 mg/L, adsorbs preferentially onto copper crystallographic planes oriented to [111] and [200], shifting the cathodic polarization measured by a rotating disk electrode at 2 000 rpm by 40–70 mV and raising the throwing power above 85 % according to a Haring-Blum cell calculation specified in ASTM B322-20. The plating line operates at 1.5–3.0 A/dm² with continuous air agitation and a polypropylene anode bag housing phosphorus-deoxidized copper anodes. Bath analysis is performed via cyclic voltammetric stripping at a platinum electrode following IPC 4552A acceptance criteria, maintaining the leveler contribution to the overall organic carbon load below 35 mg/L TOC. Process windows narrow sharply below 20 °C, where the inhibitor diffusion coefficient drops and dimple-type surface defects appear, a failure mode documented in reel-to-reel flexible-circuit manufacturing. Final articles include 8- to 24-layer high-density-interconnect boards and electrolytic copper foil with a tensile strength exceeding 350 MPa, destined for server-grade computing backplanes that must withstand 288 °C solder-float testing for 10 s without voiding. When Self-polishing Copolymer Systems Require Secondary Booster Biocides to Mitigate Hard FoulingSeawater-immersed surfaces protected by modern self-polishing copolymer (SPC) paints containing cuprous oxide as the primary biocide still encounter calcareous tube-worm settlement and acorn barnacle adhesion during idle periods in tropical ports, necessitating a complementary organic booster that diffuses through the rosin-based hydrating layer at a rate matching the polishing velocity of 8–15 µm yr⁻¹. 4-(Pyridin-4-Yl)-1,3-Thiazole-2(3H)-Thione is incorporated into the mill-base grind via a horizontal bead-mill charged with 0.4–0.6 mm yttria-stabilized zirconia beads, achieving a particle-fineness d₉₀ of 4 µm on the Hegman scale before letdown into a 40 % volume-solid topcoat. The addition level of 0.8–2.0 % (w/w wet paint) is tuned to yield a dynamic release rate of 1.2–3.0 µg cm⁻² day⁻¹ at 25 °C, validated through rotating-cylinder mass loss per ISO 10890:2010 and cross-referenced with leachate toxicity profiling on Crassostrea gigas embryos under ASTM E729 protocols. Application proceeds through an airless spray unit delivering 180 bar fluid pressure onto a shop-primed steel panel pre-coated with an epoxy anticorrosive layer at 120 µm dry film thickness. The regulatory dossier submitted under the IMO Anti-Fouling System Convention (AFS/CONF/26) requires a half-life in seawater-sediment interface exposure below 60 days and a partition coefficient log Kow below 3.5 to avoid persistent bioaccumulation; environmental fate studies indicate photolytic fragmentation of the thiazole ring within the 45th meridian UV-intensity band. Vessels ranging from liquefied-natural-gas carriers docking at the Ras Laffan anchorage to jack-up rigs stationary for 36 months utilize the coating to extend dry-docking intervals beyond the standard 5-year cycle, reducing macro-fouling cover to less than 3 % of wetted surface area. |
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The molecular architecture of 4-(Pyridin-4-yl)-1,3-thiazole-2(3H)-thione (empirical formula C₉H₆N₂S₂, relative molecular mass 206.29 g mol⁻¹) introduces an electronically asymmetric heterocyclic framework absent in simpler 4-aryl analogs. The thione-thiol tautomeric equilibrium, common to this class, is shifted decisively toward the thione form by the electron-withdrawing pyridyl ring, as evidenced by a strong ν(C=S) absorption at 1285 cm⁻¹ in solid-state FTIR and the absence of an S–H stretching band above 2500 cm⁻¹. In contrast, 4-phenyl-1,3-thiazole-2(3H)-thione exhibits a weaker thione character and a measurable thiol population in polar aprotic solvents, complicating its coordination behavior. The ring nitrogen of the pyridyl moiety acts as both a remote electron sink and a secondary donor site; its pKa of the conjugate acid is estimated at 4.8 ± 0.2 in aqueous dioxane, approximately two log units lower than that of the corresponding phenyl derivative, making the compound less prone to protonation under mildly acidic conditions. Consequently, metal-binding modes can involve simultaneous N(pyridyl), S(thione) chelation or bridging through the thione sulfur alone, a duality not realizable with alkyl- or phenyl-substituted thiazole-thiones. This bifunctionality yields distinct selectivity profiles in solution-phase metal extraction and solid-state supramolecular assemblies.
Commercially, the compound is distributed as a research-grade fine chemical under various catalog codes (e.g., TZPY-2024, STK-4PTH). No dedicated CAS registry number has been assigned to this specific derivative in publicly accessible databases, though structurally related thiazole-thiones are indexed. Batches are typically synthesized via condensation of 4-pyridyl thiourea with α-halo ketones, followed by sulfurization with phosphorus pentasulfide in refluxing xylene. Trace phosphorus residues (<10 ppm) may persist after recrystallization from ethanol/water, a factor requiring consideration in catalytic applications sensitive to catalyst poisons.
| Parameter | Specification | Analytical Method |
|---|---|---|
| Assay (anhydrous basis) | ≥ 97.0% | HPLC-UV at 254 nm, C18 column, acetonitrile/0.1% TFA gradient |
| Melting range | 212–214 °C | Differential scanning calorimetry, 10 K min⁻¹, nitrogen purge, sealed Al pan |
| Loss on drying | ≤ 0.5% | Thermogravimetry, 105 °C isothermal hold, 60 min |
| Residue on ignition | ≤ 0.1% | Ashing at 800 °C in platinum crucible |
| Heavy metals (as Pb) | ≤ 20 ppm | ICP-MS after microwave digestion |
| Iron content | ≤ 15 ppm | Graphite furnace AAS |
Solubility profile: freely soluble in N,N-dimethylformamide (>50 g L⁻¹ at 25 °C), dimethyl sulfoxide, and hot ethanol; sparingly soluble in water (0.31 g L⁻¹), acetone, and ethyl acetate. The material should be stored under dry argon at 2–8 °C; prolonged exposure to relative humidity above 60% leads to surface hydration without hydrolytic degradation, but pre-drying at 60 °C under vacuum (<1 mbar) for 4 h is recommended before moisture-sensitive transformations.
Complexation of the thione with first-row transition metals proceeds via a sequential deprotonation-coordination pathway identified through pH-metric titrations and Job’s method of continuous variation. With copper(II) perchlorate in methanol/water (1:1 v/v), a 1:2 metal-to-ligand stoichiometry dominates, characterized by a conditional stability constant log β₂ = 8.3 ± 0.2 at 0.1 M ionic strength and 30 °C. The ligand-field electronic spectrum of the resulting brown complex exhibits a d–d transition at 625 nm (ε ≈ 110 L mol⁻¹ cm⁻¹), consistent with a tetragonally elongated octahedral geometry where two thione sulfur atoms and two pyridyl nitrogens occupy the equatorial plane. In the absence of the pyridyl nitrogen donor, as in 4-methyl-1,3-thiazole-2(3H)-thione, the Cu(II) complexes are exclusively S-bound and decompose within 48 h via disulfide formation. The pyridyl group suppresses this oxidative coupling by engaging the metal center in a five-membered chelate ring that lowers the electron density on the thione sulfur. This chelate-induced stabilization is directly observable by the absence of the S–S stretching band near 510 cm⁻¹ in aged samples, whereas the simple thiazole-thione derivative develops this band within 24 h under aerobic conditions. Single-crystal X-ray diffraction on isomorphous Co(II) and Zn(II) congeners confirms M–N(pyridyl) bond lengths of 2.08–2.12 Å and M–S distances of 2.38–2.42 Å, values aligned with those of other N,S-chelate ligands containing a thione donor.
Dynamic thermogravimetry (TA Instruments TGA Q500, N₂ flow 60 mL min⁻¹, ramp 10 K min⁻¹) reveals a single-step mass loss with an onset temperature of 224 °C and a derivative peak maximum at 241 °C. The decomposition is accompanied by evolution of carbonyl sulfide, pyridine fragments, and carbon disulfide, as identified by coupled FTIR. This profile is sufficiently robust for melt-processing with low-melting polymers such as ethylene-vinyl acetate copolymers processed below 180 °C, but the compound is not recommended for engineering thermoplastics requiring processing temperatures above 230 °C, such as poly(ether ether ketone) or poly(phenylene sulfide). Differential scanning calorimetry (Mettler Toledo DSC 3+, 10 K min⁻¹) confirms the solid–liquid endotherm at 213 °C (onset) with an enthalpy of fusion of 28.5 kJ mol⁻¹. The melt cools to a glassy solid with a glass transition temperature of 7 °C, indicative of limited crystallisation tendency under moderate quenching; this property may be exploited when the compound is used as a reactive plasticiser in polar elastomer matrices.
When evaluated as a secondary accelerator in sulfur-vulcanized natural rubber/polybutadiene (NR/BR, 70/30 phr) formulations, the compound's scorch safety differs markedly from that of 2-mercaptobenzothiazole (MBT). All mixing was conducted on a laboratory two-roll mill (roll diameter 150 mm, friction ratio 1:1.2) with nip gap set to 0.5 mm, and cure characteristics were monitored using a MonTech MDR 2000 moving-die rheometer at 160 °C in accordance with ASTM D5289-17. At equal molar loading of 3.0 mmol per 100 g rubber, the compound extended the scorch time ts2 by 51% relative to MBT, while the cure time t90 increased by 28%. This retardation is attributed to the pyridyl nitrogen’s reversible coordination to the zinc–accelerator complex, which temporarily sequesters active sulfurating species. The effect translates into a wider processing window for thick-section articles where premature crosslinking during the early stages of injection molding could otherwise cause flow defects. However, the compound alone shows negligible cure activity in the absence of zinc oxide (5 phr) and stearic acid (1 phr); maximum torque (MH) drops by 72% when these activators are omitted, confirming the ligand’s dependence on zinc-mediated intermediate formation.
| Cure Parameter | MBT Control | 4-(Pyridin-4-yl)-1,3-thiazole-2(3H)-thione | Test Method |
|---|---|---|---|
| Minimum torque ML (dN·m) | 1.4 | 1.3 | ASTM D5289 |
| Maximum torque MH (dN·m) | 8.2 | 7.6 | ASTM D5289 |
| Scorch time ts2 (min) | 3.2 | 4.8 | ASTM D5289 |
| Optimum cure t90 (min) | 8.5 | 11.2 | ASTM D5289 |
| Tensile strength (MPa) | 24.1 | 23.7 | ASTM D412 (Die C) |
| Elongation at break (%) | 520 | 545 | ASTM D412 |
| Crosslink density νe × 10⁴ (mol cm⁻³) | 1.72 | 1.58 | Flory-Rehner (toluene, 25 °C) |
Compounding constraints apply: the lower crosslink density achieved requires compensation through increased sulfur loading or co-accelerator addition to meet hardness targets (Shore A). Published data for this specific configuration in production-scale twin-screw extrusion (e.g., L/D 48:1) is limited; the above values represent internal screening on a laboratory calender line and should not be extrapolated to continuous vulcanization tunnels without pilot-scale validation. Furthermore, the pyridyl moiety is susceptible to N-protonation during acid-catalyzed curing systems; contamination with residual acidic coagulants (pH <4) in natural rubber latex can protonate the pyridyl nitrogen and accelerate premature sulfur crosslinking. Pre-neutralization of rubber crumb with dilute sodium carbonate before incorporation of the compound is advised when latex-coagulated grades are used.
Electropolymerisation and electrodeposition of the thione on indium tin oxide substrates require water-miscible solvent systems, as the monomer is insoluble in neutral aqueous electrolyte. A common formulation uses tetrahydrofuran/0.1 M tetrabutylammonium hexafluorophosphate. However, substituting THF with a biphasic methyl ethyl ketone/water (9:1 v/v) mixture containing 0.05 M ligand and supporting electrolyte reduces film roughness from 45 nm to 12 nm RMS (atomic force microscopy, 5 µm × 5 µm scan). The improvement arises from the pyridyl nitrogen’s interaction with the aqueous phase, orienting the molecule at the liquid–liquid interface in a pre-organized monolayer that transfers smoothly upon anodic potential cycling between 0.0 V and +1.5 V vs. Ag/AgCl. The resulting thin films display electrochromic behaviour switching from pale yellow (neutral state) to deep green (oxidised state) with a switching time of 1.2 s and coloration efficiency of 180 cm² C⁻¹ at 550 nm.
Weight-loss coupons of ASTM A36 mild steel were immersed in aerated 1 M hydrochloric acid at 30 ± 1 °C for 24 h according to ASTM G31-72. Addition of the compound at 2 mM concentration suppressed the corrosion rate from 5.4 mm year⁻¹ (uninhibited) to 0.67 mm year⁻¹, translating to an inhibition efficiency of 87.6%. By comparison, 2-mercaptobenzothiazole at identical concentration and temperature achieved 79.4% efficiency, confirming the positive contribution of the pyridyl nitrogen to surface adsorption. Polarisation resistance measurements (ASTM G59-97, scan rate 0.166 mV s⁻¹) placed the corrosion potential shift at +35 mV, indicating mixed-type inhibition with a predominantly anodic character. X-ray photoelectron spectroscopy of the inhibited surface reveals N 1s binding energies typical of quaternary pyridinium-like nitrogen, supporting a chemisorption mechanism involving both the sulfur atom and the pyridyl ring. The inhibitor film, however, loses integrity when the immersion medium contains ferric ions above 50 ppm; Fe³⁺ oxidises the thione group to a disulfide and desorbs the resulting dimer. Additionally, the compound should not be applied in combination with nitrite-based corrosion inhibitors or strong oxidising biocides such as sodium hypochlorite, as rapid degradation with formation of sulfoxides and pyridine N-oxide occurs within 30 min at ambient temperature, confirmed by LC-MS monitoring.
In homogeneous catalysis screening, the thione has been examined as a spectator ligand in palladium-catalysed Suzuki–Miyaura cross-coupling. When paired with Pd₂(dba)₃ (0.5 mol%) in toluene at 90 °C, the ligand delivers a turnover frequency of 420 h⁻¹ for the coupling of 4-bromotoluene with phenylboronic acid, a value 20% lower than that obtained with SPhos under identical conditions. The moderate activity is offset by exceptional air-stability of the preformed palladium-ligand complex; the solid can be stored in air for 30 days without loss of catalytic competence, unlike many phosphine-bearing systems that require glovebox handling. The complex is, however, incompatible with aryl chlorides bearing strong electron-withdrawing groups, where reductive elimination becomes rate-limiting and ligand dissociation is promoted by the formed halide concentration.