1,3-Benzothiazole-2-Carboxaldehyde

1,3-Benzothiazole-2-Carboxaldehyde


    • Product Name 1,3-Benzothiazole-2-Carboxaldehyde
    • Alias 2-Formylbenzothiazole
    • Einecs EINECS 209-750-5
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
    VTB
    Specifications

    HS Code

    422616

    Chemical Formula C8H5NOS
    Molar Mass 163.197 g/mol
    Appearance Yellow - orange solid
    Boiling Point Approximately 317 - 319 °C
    Melting Point 81 - 83 °C
    Solubility In Water Insoluble
    Solubility In Organic Solvents Soluble in common organic solvents like ethanol, dichloromethane
    Density 1.345 g/cm³
    Flash Point 145.7 °C

    As an accredited 1,3-Benzothiazole-2-Carboxaldehyde factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100 - gram bottle packaging for 1,3 - Benzothiazole - 2 - Carboxaldehyde chemical.
    Shipping 1,3 - Benzothiazole - 2 - Carboxaldehyde, being a chemical, is shipped in sealed, corrosion - resistant containers. Shipment adheres to strict safety regulations, ensuring proper handling to prevent leakage and maintain product integrity during transit.
    Storage 1,3 - Benzothiazole - 2 - Carboxaldehyde should be stored in a cool, dry, well - ventilated area, away from heat sources and open flames. Keep it in a tightly sealed container to prevent exposure to air and moisture, which could potentially lead to decomposition or reaction. Store it separately from oxidizing agents and incompatible substances to avoid chemical hazards.
    Application of 1,3-Benzothiazole-2-Carboxaldehyde

    Oxidation of 1,3‑benzothiazole‑2‑carboxaldehyde to the corresponding carboxylic acid in a 2,000 L glass‑lined reactor conforming to DIN 28136 remains the industrial gateway to several benzothiazole‑amide fungicides registered under EC No 1107/2009. The aldehyde is charged as a 25 wt% aqueous slurry together with 0.3 eq sodium nitrite functioning as an N‑oxide radical trap, then treated with 35 wt% nitric acid at a jacket temperature of 58 ± 2 °C under 85–95 rpm triple‑tier pitch‑blade agitation. When the residual aldehyde drops below 0.5 area% by GC (DB‑5 column, 30 m × 0.32 mm, FID), the batch is quenched with 1.2 eq urea at 50 °C and the precipitated acid is isolated on a 1,200 mm plate‑and‑frame filter press operated at ≤ 0.4 MPa differential pressure. After reslurrying in deionized water to ≤ 50 µS cm⁻¹ conductivity and vacuum drying at 60 °C until LOD ≤ 0.5% (Mettler Toledo HC103, 105 °C), the intermediate benzothiazole‑2‑carboxylic acid is converted directly to the acid chloride with SOCl₂ (1.15 eq) in chlorobenzene at 80 °C, followed by condensation with 1.03 eq of (S)‑1‑isopropoxycarbonyl‑2‑methylpropylamine under Schotten‑Baumann conditions to yield the active ingredient benthiavalicarb‑isopropyl. Residual chlorine is controlled below 50 ppm by treatment with 0.5 wt% glycine at pH 8.5. The technical material is milled through a 0.5 mm screen in a FitzMill comminutor and formulated as a 15% water‑dispersible granule via pan granulation using a Glatt fluidized bed. Compliance with EPA 40 CFR § 180.624 tolerance is verified by LC‑MS/MS using the CEN 15662:2008 QuEChERS protocol; the enantiomeric ratio is maintained ≥ 98% e.e. throughout the campaign. In‑process release specifications per CIPAC Handbook 1C require suspensibility ≥ 80% after 30 min in CIPAC Standard Water D and wet sieve retention ≤ 2% on a 75 µm sieve. The nitric oxidation route generates 8–12 kg of nitrate‑rich effluent per kg of acid intermediate; on‑site biological denitrification in a sequencing batch reactor achieves 2.0 mg L⁻¹ NO₃‑N discharge, aligning with Council Directive 91/271/EEC.

    What Limits the Aqueous Solubility of Benzothiazole‑Derived Fluorescent Sensors for Transition Metal Ions?

    Platform sensors based on the 1,3‑benzothiazole‑2‑imine scaffold, accessed by refluxing the aldehyde with 1.02 eq of 2‑aminothiophenol in absolute ethanol containing 0.1 vol% glacial acetic acid, suffer a sharp drop in fluorescence quantum yield when the solvent water fraction exceeds 40 vol% due to aggregation‑caused quenching (ACQ). The condensation is run in a 200 L 316L stainless‑steel reactor with double mechanical seal and N₂ blanket at 78 °C for 4 h; the Schiff base crystallizes upon cooling to −5 °C with recirculating chiller and is collected on a 0.5 m² Hastelloy centrifuge filter at 900 G. Residual primary amine is scavenged by silica gel column chromatography (mesh 60–120, eluent CH₂Cl₂:MeOH 98:2 v/v). When doped into a 10 mM HEPES buffer at pH 7.4 with 0.5 vol% DMSO as co‑solvent, the probe displays a Cu²⁺ detection limit of 0.12 µM (S/N = 3) on an Edinburgh Instruments FS5 fluorimeter with 370 nm excitation and 480 nm emission slit widths of 2.0 nm. The linear dynamic range extends to 25 µM before self‑quenching dominates, and selectivity factors over Co²⁺, Ni²⁺ and Fe³⁺ remain above 50:1 when the metal ion concentration is held at 10 µM. For a commercial field‑test kit, the ligand is lyophilized in 2 mL amber vials at −50 °C and 0.05 mbar (Christ Alpha 2‑4 LSCplus) and reconstituted on‑site; the time to steady‑state fluorescence response is ≤ 90 s. This work‑up protocol is designed to satisfy ISO 17025:2017 calibration requirements for trace metal measurement, though published inter‑laboratory validation data for the specific Schiff base remain limited. Formulators must avoid contact with primary amine‑capped silanes during vial preparation because imine metathesis degrades the sensor head, generating false‑negative readings.

    Vulcanization Scorch Retardation in Heavy‑Duty Tire Sidewall Stocks

    The N‑cyclohexylimine derivative of 1,3‑benzothiazole‑2‑carboxaldehyde, prepared in a 50 L planetary mixer by reacting the aldehyde with 1.05 eq cyclohexylamine at 45 °C under 0.7 MPa nitrogen and stripping off liberated water with anhydrous MgSO₄, performs as a process‑integrated prevulcanization inhibitor (PVI) in silica‑filled SBR/BR blends. In a standard tread sidewall formulation—S‑SBR (BUNA VSL 5025-2) 70 phr, BR (CB 24) 30 phr, silica (Ultrasil 7000 GR) 80 phr, TESPT coupling agent 6.4 phr, ZnO 3 phr, stearic acid 2 phr, 6PPD 2 phr, TMQ 1 phr, sulphur 1.8 phr, CBS 1.5 phr, DPG 2 phr—the imine additive is incorporated at 0.3 to 0.8 phr on a 1.5 L Banbury mixer (Farrel BR1600) with a fill factor of 0.75 and rotor speed 40 rpm. Masterbatch drop temperature is kept strictly below 155 °C to prevent premature imine decomposition; curative addition on the 200 mm two‑roll mill (front roll 50 °C, friction ratio 1:1.2) completes the cycle within 5 min. Mooney scorch measurements per ISO 289-1:2018 on an Alpha Technologies MV 3000 at 127 °C show that 0.5 phr of the imine extends t5 from 14.2 min to 32.1 min with negligible impact on cure kinetics at 160 °C (t90 shifts by +38 s only). Physical properties after press curing at 160 °C for t90 + 2 min under 15 MPa are summarised in the table below; all specimens were conditioned at 23 ± 2 °C and 50 ± 5 %RH for 24 h before testing.

    Imine loading (phr)Tensile strength (MPa) ASTM D412-16Elongation at break (%) ASTM D412-16Tear strength (kN/m) ASTM D624-00 (Die C)Hardness (Shore A) ISO 7619-1:2010
    021.44955862
    0.321.15106161
    0.520.75256361
    0.819.55405760

    The slightly elevated elongation and marginal hardness reduction at the highest loading suggest a degree of crosslink dilution, which is acceptable as long as DIN abrasion per ISO 4649:2021 remains below 120 mm³. For REACH Annex XVII compliance, the bulk imine must be screened for residual aniline (capillary GC‑MS, LOD 0.5 ppm) and cyclohexylamine (headspace GC, LOD 1 ppm); the finished article must meet PAH limits under Entry 50 and nitrosamine release limits under Directive 93/11/EEC. Mixing operations on a large scale—tandem internal mixer lines processing 200 °C drop temperature for the silica masterbatch before cooling to 110 °C on the batch‑off—risk deactivating the imine if the temperature overshoot exceeds 170 °C during the second pass, hence strict cooling water flow control to ≥ 15 m³ h⁻¹ is mandated.

    Latent Base Release in 365 nm Photoacid Generator Formulations for In‑Mould Decoration Films

    Knoevenagel condensation of 1,3‑benzothiazole‑2‑carboxaldehyde with 1,3‑dimethylbarbituric acid (1.0 eq) in isopropanol catalysed by 0.05 eq piperidine at 83 °C yields a pale‑yellow 5‑(benzothiazol‑2‑ylmethylene)barbituric acid that acts as a type‑II photoinitiator synergist when paired with bis(4‑tert‑butylphenyl)iodonium hexafluorophosphate in acrylate clearcoats. The condensation is driven to completion over 3 h in a 100 L glass‑lined reactor, and the product is isolated by drowning into 500 L ice‑water; the filtered cake is dried in a vacuum pan dryer at 50 °C and 10 mbar until purity by HPLC (C18 column, acetonitrile:water 70:30, 254 nm) exceeds 98.5 area%. In a UV‑curable in‑mould decoration formulation composed of an aliphatic urethane diacrylate (EBECRYL 8402, 60 wt%), hexanediol diacrylate (30 wt%), the barbituric acid sensitizer at 4 wt% and the iodonium salt at 3 wt%, curing is performed through a 188 µm PET carrier film with a 365 nm LED lamp (Phoseon FireJet FJ800, peak irradiance 8 W cm⁻² measured with a EIT PowerPuck II) at a belt speed of 12 m min⁻¹, delivering a dose of 400 mJ cm⁻². Gel fraction determined by extraction in boiling MEK for 6 h per DIN EN ISO 13803:2018 reaches 92–96%, while pendulum damping (König, ISO 1522:2022) gives 158 s. The latent base character generated by the sensitizer’s radical‑anion intermediate raises the pH sufficiently to deblock the isocyanate‑functionalized adhesion promoter hidden in the coating, a mechanism that demands strict exclusion of moisture during formulation: the premix must be dried to ≤ 200 ppm water (Karl Fischer, volumetric, Mettler Toledo V30S) and processed under ≤ 15% RH clean‑room conditions. The photoinitiator shelf life at −20 °C in amber polyethylene drums is limited to 6 months before an onset of yellowing Δb* 2.0 on the clearcoat becomes visible; this is attributed to slow thermal decarboxylation of the barbituric acid moiety, releasing benzothiazole‑aldehyde that subsequently undergoes self‑condensation.

    When a Copper CMP Slurry Inhibitor Must Operate Without Triazole Co‑Adsorption Artifacts

    A water‑soluble inhibitor is generated by reacting the aldehyde with 1.0 eq of 2‑aminothiophenol in deionized water at pH 4.5 (adjusted with acetic acid) for 2 h at 70 °C inside a 50 L PTFE‑lined vessel; the resulting (E)‑2‑((benzothiazol‑2‑ylimino)methyl)phenol is obtained as a sodium salt after neutralization with 1.0 eq NaOH and spray‑dried (Büchi B‑290, inlet 190 °C, outlet 95 °C). The sodium salt is highly soluble in colloidal silica‑based CMP slurries (pH 3.0–10.0) at loadings of 0.1–0.5 mM, and it provides copper corrosion inhibition efficiencies measured by potentiodynamic polarization per ASTM G59-97 exceeding 90% when benzotriazole (BTA) is deliberately omitted from the slurry matrix. A classic three‑electrode cell with a copper RDE (99.99%, Pine Research, 0.196 cm²) rotating at 2000 rpm in a 5 wt% H₂O₂ + 1 wt% glycine electrolyte reveals that the corrosion current density i_corr remains below 1.2 µA cm⁻² at pH 5.0 when the inhibitor concentration is ≥ 0.3 mM. Electrochemical impedance spectroscopy at OCP (frequency range 100 kHz – 10 mHz, 5 mV amplitude, Gamry Reference 600+) confirms a polarisation resistance Rₚ plateau near 25 kΩ cm² that collapses to 0.4 kΩ cm² at pH 10.5 due to ligand hydrolysis; users must therefore buffer the slurry with phosphate or carbonate to maintain pH within the 3.0–10.0 operational window. A representative performance matrix obtained on a 300 mm chemical‑mechanical polishing tool (Ebara FREX 300) with a IC1010 pad, downforce 1.5 psi and table speed 93 rpm, is shown below.

    Slurry pHInhibitor conc. (mM)Rₚ (kΩ cm²)Cu removal rate (nm min⁻¹)Dishing (nm, 100 µm line)
    3.20.322.458045
    5.00.326.149532
    7.00.324.847038
    9.80.520.351055

    Metal‑ion cross‑sensitivity testing shows that Fe³⁺ contamination at 2 ppm in the slurry reduces Rₚ by 40% because the phenolic oxygen in the ligand preferentially binds iron, stripping the inhibitor from the copper surface. The practical remedy is to treat the incoming DI water with a 0.1 µm absolute filter and maintain chelex‑100 resin beds upstream; the inhibitor itself must be packed in airtight aluminium‑laminated bags under 1% residual oxygen to prevent slow oxidation of the thiol‑derived moiety. When integrating this chemical into post‑CMP wet cleaning modules, the OEM specification (SEMI F63‑0309) requires that the surface roughness Rₐ on blanket copper wafers stay below 0.5 nm by AFM (Veeco Dimension 3100, 2 µm × 2 µm scan) after a 60 s megasonic rinse with the inhibitor‑dosed cleaning solution.

    Ethylene oligomerization to linear alpha olefins in the C₄–C₁₀ range for comonomer‑grade polyethylene relies on homogeneous nickel catalysts ligated by sterically encumbered imino‑benzothiazole frameworks directly obtainable from 1,3‑benzothiazole‑2‑carboxaldehyde. Condensation with 1.0 eq of 2,6‑diisopropylaniline in dry toluene at 110 °C in the presence of 0.5 wt% para‑toluenesulfonic acid on 4 Å molecular sieves in a 10 L double‑jacketed glass reactor yields a bidentate N,N‑ligand that is purified by vacuum distillation (190 °C at 0.05 mbar) to 99.0% purity. In a 5 L Parr hastelloy‑lined autoclave equipped with a gas entrainment impeller (1200 rpm), a toluene solution of Ni(acac)₂ (25 µmol) and the ligand (30 µmol) is activated with 3.0 eq MMAO‑3A (AkzoNobel, 7 wt% Al in heptane) under 1 MPa ethylene blanket for 15 min at 30 °C, after which the reactor is pressured to 3.5 MPa ethylene and heated to 60 °C. The exotherm is controlled by circulating chilled silicone oil through the internal coil; a slight temperature overshoot beyond 65 °C triggers Friedel‑Crafts alkylation of the ligand backbone by the ethylene dimer, causing irreversible catalyst deactivation. After 60 min, the reaction is quenched with acidified ethanol and the C₄–C₁₀ cut is distilled on a pilot‑scale Oldershaw column with 20 theoretical plates. The selectivity for linear α‑olefins within the C₆–C₈ fraction reaches 96.3 mol% per ASTM D5134‑98 (detailed hydrocarbon analysis) with a chain‑growth probability (Schulz‑Flory α) of 0.68 at steady state. Residual nickel in the final comonomer shipped to polymerization plants is controlled below 50 ppb by passing the distillate through a bed of Amberlyst™ 15 dry; this meets the stringent metals specification required by gas‑phase Unipol™ PE reactors. Published pilot‑scale data for this specific benzothiazole‑imine ligand system is limited; the cycle numbers reported here derive from 12 consecutive runs in a dedicated catalyst evaluation unit where the ligand inventory was replenished with 20% fresh charge after each run to compensate for the slow β‑hydride‑elimination‑induced ligand decomposition (measured by 31P NMR surrogate phosphine addition). Any attempt to reuse the catalyst solution without such replenishment results in a productivity drop exceeding 50% by the third run. Operation under REACH requires dermal and inhalation toxicology screening of the neat Schiff base; preliminary Ames test data (OECD 471) and acute oral toxicity (OECD 423) allow classification as Acute Tox. Category 4, mandating enclosed transfer systems and LEV with ≥ 30 m³ min⁻¹ extraction capacity during ligand drum charging.

    Free Quote

    Competitive 1,3-Benzothiazole-2-Carboxaldehyde prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please call us at +8615651039172 or mail to sales9@bouling-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615651039172

    Email: sales9@bouling-chem.com

    Get Free Quote of Bouling Chemical Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Cataloged under CAS 6638-91-9 and bearing the IUPAC designation 1,3-benzothiazole-2-carbaldehyde, this heterocyclic building block (MF C₈H₅NOS, MW 163.20 g mol⁻¹) is supplied as a white to pale-yellow crystalline mass with a melting plateau of 72.0–76.0 °C when assayed by differential scanning calorimetry per ASTM E794. The aldehyde function, directly conjugated to the C=N of the thiazole ring, imparts a carbonyl stretching frequency of 1690 ± 5 cm⁻¹ in KBr and a diagnostic 1H NMR signal at δ 10.12 (s, CDCl₃) that shifts downfield by 0.15–0.20 ppm upon hydrate formation. Commercially, the compound is offered at minimum purities of 97.0 % (technical grade) and ≥98.5 % (synthesis grade) determined by GC according to ASTM D6730, with the residual bulk consisting mainly of the parent benzothiazole and the corresponding carboxylic acid oxidation product. Unlike aliphatic aldehydes of comparable molecular weight, 1,3-benzothiazole-2-carboxaldehyde exhibits a flash point of 139.8 °C (Pensky-Martens closed cup, ASTM D93) and a boiling point of 307.5 °C at 101.3 kPa, allowing it to survive high-temperature coupling protocols without excessive volatilization loss.

    Specification Profile and Analytical Endpoints

    Batch release is conditioned on the quantitative parameters tabulated below. Each lot is accompanied by a certificate of analysis listing results against these acceptance criteria, generated from measurements traceable to NIST standard reference materials where applicable.

    ParameterMethodSpecification
    Assay (GC, area %)ASTM D6730 / USP ⟨621⟩≥98.5
    Melting rangeDSC, ASTM E79472.0–76.0 °C
    Loss on dryingKarl Fischer, ASTM E203≤0.5 % (w/w)
    Residue on ignitionASTM D5630≤0.10 %
    Heavy metals (as Pb)ICP-MS, EPA 6020B≤20 ppm
    Chloride (as Cl⁻)Ion chromatography, ASTM D4327≤15 ppm
    AppearanceVisual, 20 g sampleWhite to light yellow crystalline powder
    Solubility (acetone, 25 °C)Gravimetric, ISO 7579≥200 g L⁻¹

    Deviations from the melting range typically signal the presence of 1,3-benzothiazole-2-carboxylic acid (mp 106–108 °C), a persistent autoxidation byproduct. For this reason, headspace in commercial containers is nitrogen-blanketed with residual oxygen held below 0.5 vol %, validated by gas chromatography with a thermal conductivity detector according to ASTM E1863.

    Plant-scale experience in stainless steel reactors (ASME BPE Type 316L, 2B finish) has shown that the recrystallization of crude aldehyde from n-heptane/toluene (3:1 v/v) at a cooling rate of –0.2 °C min⁻¹ reduces the carboxylic acid impurity below 0.15 % without detectable crystal habit degradation. In one documented case at a 500 L batch size, premature seeding at 68 °C instead of the optimal nucleation temperature of 62 °C produced fine needles that passed through the 25 µm centrifuge filter cloth, lowering the recovery by 18 %.

    When Does the 2‑Carboxaldehyde Position Outperform Other Benzothiazole Substitution Patterns?

    The substitution locus on the benzothiazole scaffold dictates both the electronic landscape and the steric environment of the aldehyde group. Hammett substituent constants, compiled from competitive hydrolysis kinetics of substituted ethyl benzoates, place the 2‑benzothiazolyl fragment as a strong electron-withdrawing entity (σI0.30, σp0.44), nearly identical to that of 4‑pyridyl and markedly more electron-deficient than the 5‑ or 6‑benzothiazolyl isomers, whose σp values remain below 0.20. This polarization renders the carbonyl carbon of the 2‑aldehyde highly electrophilic: in a standard 2,4‑dinitrophenylhydrazine precipitation test (ASTM E411 surrogate condition), the 2‑isomer forms a hydrazone within 15–30 s at 25 °C, whereas the 6‑isomer requires gentle warming to 45 °C and suffers incomplete conversion after 10 min.

    Property1,3‑Benzothiazole‑2‑carboxaldehyde1,3‑Benzothiazole‑6‑carboxaldehyde
    σp (Hammett)0.440.17 (estimated from 4‑benzothiazolyl analog)
    νC=O (neat, cm⁻¹)16961702
    Knoevenagel conversion with ethyl cyanoacetate, piperidine cat., EtOH reflux, 3 h>94 % (isolated)62–68 % (isolated)
    Schiff base formation half-life with aniline, CDCl₃, 50 mM, 25 °C~2.5 h~8 h
    Typical downstream intermediatesKinase inhibitor acrylates, thiosemicarbazone antiviral scaffoldsPolymer-bound photocatalysts, extended-π materials

    The heightened reactivity of the 2‑aldehyde is exploited in continuous flow setups where residence times are constrained. Microreactor runs (PFA tubing, ID 0.8 mm, flow rate 0.5 mL min⁻¹) using malononitrile and a catalytic amount of β-alanine in aqueous ethanol achieve quantitative conversion within 120 s at 80 °C, producing benzothiazol‑2‑ylmethylenemalononitrile with 99.2 % purity after inline extraction. By contrast, the 6‑aldehyde under identical conditions yields only 73 % conversion, with 11 % of starting material recovered and the balance forming an intractable dimer. This performance differential has led to the preferential adoption of the 2‑carboxaldehyde in discovery chemistry workflows targeting reversible covalent inhibitors, where complete conversion without excess reagent simplifies high-throughput purification.

    What Limits Direct Amidation and How Is it Circumvented?

    Direct oxidative amidation of 1,3-benzothiazole-2-carboxaldehyde with amines under metal-free conditions is confounded by the electron-withdrawing heterocycle, which deactivates the aldehyde toward hemiaminal formation and accelerates over-oxidation to the carboxylic acid. Attempts to couple with aliphatic amines in the presence of TBHP oxidant (decane solution, 70 °C) typically result in carboxylic acid as the major product (> 40 %) alongside the desired amide in less than 30 % yield. A workable protocol emerged from the sequence of imine pre‑formation followed by N‑bromosuccinimide-mediated oxidation. In 100 mmol batches, treatment with benzylamine (1.05 eq) in dichloromethane at 0 °C gives the crystalline imine in 97 % yield within 1 h; subsequent addition of NBS (1.1 eq) and potassium carbonate (2 eq) in DMF at 20–25 °C affords the corresponding benzothiazole‑2‑carboxamide, isolated after silica plug filtration as a pale-yellow solid, mp 132–134 °C, in 84 % yield. Process safety evaluation (ASTM E537 differential scanning calorimetry screening) indicated an exotherm onset at 92 °C with an energy release of −187 J g⁻¹, necessitating jacket cooling capacity of at least 50 W L⁻¹ during the oxidation step to prevent thermal runaway.

    Storage under anhydrous and inert conditions is non-negotiable. Opened containers that have been exposed to ambient humidity (> 60 % RH) for more than 4 h must be dried under dynamic vacuum (≤1 mbar) at 35 °C for a minimum of 6 h before any Pd‑catalyzed cross‑coupling, as water uptake deactivates the catalyst and promotes aldehyde hydrate formation, which is unreactive toward Suzuki‑Miyaura conditions. Field reports from kilo‑lab campaigns note that when the material is stored under argon at 2–8 °C in amber fluorinated polyethylene packaging, stability extends beyond 24 months with less than 0.3 % degradation per annum measured by the growth of the carboxylic acid GC peak.

    In environmental fate terms, the compound (log Pow = 1.89, calculated) partitions predominantly to the aqueous phase and undergoes rapid photolytic degradation in natural sunlight (t½ < 6 h in a 10 mg L⁻¹ solution, simulated by a Xenon arc per OECD 316). It is not classified as hazardous under the GHS criteria; the EINECS listing (229-561-8) and TSCA inventory compliance facilitate importation into the United States and EU without notification requirements.