Tantalum(V) Ethoxide

    • Product Name: Tantalum(V) Ethoxide
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
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    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 495633
    Name Tantalum(V) Ethoxide
    Synonyms Tantalum pentaethoxide; Tantalum ethoxide; Pentaethoxytantalum
    Casnumber 6074-84-6
    Ecnumber 228-010-3
    Molecularformula C10H25O5Ta
    Linearformula Ta(OC2H5)5
    Molecularweight 406.25 g/mol
    Appearance Colorless to pale yellow liquid
    Physicalstateat25c Liquid
    Density 1.566 g/mL at 25 °C
    Boilingpoint 145-147 °C at 0.1 mmHg
    Meltingpoint 21 °C
    Refractiveindex n20/D 1.505
    Flashpoint 87 °C (190 °F)
    Solubility Soluble in organic solvents such as ethanol, ether, and benzene; reacts with water
    Waterreactivity Hydrolyzes/reacts with water
    Sensitivity Moisture sensitive
    Storageconditions Store under inert gas; keep tightly closed; protect from moisture
    Purity Commonly 99.99% trace metals basis
    Chemicalfamily Metal alkoxide

    As an accredited Tantalum(V) Ethoxide factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Tantalum(V) Ethoxide, 100 g, packaged in an amber glass bottle under inert argon, sealed with a PTFE-lined cap.
    Container Loading (20′ FCL) Tantalum(V) Ethoxide in 20′ FCL: moisture-sensitive, flammable liquid, sealed drums under inert gas, palletized, secured, labeled for ocean transport.
    Shipping Tantalum(V) ethoxide is shipped as a moisture-sensitive, flammable liquid under UN 1993, Flammable liquid, n.o.s. (Tantalum(V) ethoxide), Class 3, PG III. Use sealed, UN-approved containers with inert gas blanketing; label flammable/moisture-sensitive; keep away from water, heat, sparks, and oxidizers. Confirm classification with current SDS.
    Storage Store Tantalum(V) ethoxide in a cool, dry, well-ventilated area under inert gas (argon or nitrogen). Keep containers tightly closed, moisture-proof, and protected from heat, flames, and oxidizers. Use flammable-liquid storage cabinets if required. Avoid contact with water, acids, alcohols, and ignition sources. Maintain secondary containment, label clearly, and inspect regularly. Follow the SDS and local regulations.
    Shelf Life Tantalum(V) ethoxide is moisture-sensitive; store sealed under inert gas in a cool, dry place. Shelf life depends on package integrity.
    Application of Tantalum(V) Ethoxide

    In dynamic random-access memory capacitor fabrication, tantalum(V) ethoxide functions as a liquid precursor for Ta2O5 high-κ dielectric films in metal-insulator-metal structures. The compound is delivered from a heated stainless-steel bubbler or a direct liquid injection vaporizer; saturated vapour delivery is constrained by the precursor’s tendency to oligomerize at elevated temperature. Production-scale ALD tools for 300 mm wafers maintain source temperatures between 100 °C and 140 °C, with downstream lines held 20–30 °C above the bubbler set point to eliminate cold spots. Carrier gas and purge line purity must be held below 0.1 ppm H2O and 0.1 ppm O2 because the ethoxide ligands undergo rapid hydrolysis to insoluble oxo-alkoxide solids that accumulate in valve bodies, mass flow controllers, and showerhead orifices. A cross-flow reactor with a base pressure below 5 × 10-4 Pa is typical, and field maintenance records indicate that unheated bellows and pressure transducer ports are the primary particle nucleation points. Alternating precursor, purge, and ozone or oxygen plasma pulses are used; precursor pulse times range from 0.2 s to 2 s, purge times from 5 s to 15 s, and plasma power settings depend on reactor geometry. Substrate temperature in ozone-based thermal processes is held between 250 °C and 325 °C; lower temperatures leave residual carbon above 3 at.% by X-ray photoelectron spectroscopy, while temperatures above 350 °C initiate gas-phase decomposition and reduce step coverage in high-aspect-ratio capacitor trenches. As-deposited films are amorphous, with refractive index at 632.8 nm rising from 2.05 to 2.15 after annealing at 600 °C to 700 °C in flowing O2. Leakage current density in fully annealed MIM capacitors is commonly reported from 10-7 A/cm² to 10-6 A/cm² at 1 MV/cm, but the result is influenced by TiN electrode roughness and interface oxidation. The central process conflict is the narrow margin between adequate vapour generation and thermal ligand loss: raising source temperature to increase film growth rate shortens vaporizer residence time and produces suboxide phases with lower breakdown strength. Liquid injection systems with flash vaporizers maintain a wetted wall evaporator temperature of 120 °C to 180 °C to limit residue; routine replacement of the injection nozzle and downstream filter elements is documented in high-volume semiconductor tool logs. Handling is performed under ISO 14644-1:2015 Class 4 cleanroom conditions or better, and surface particle cleanliness is verified according to ISO 14644-9:2022.

    Representative ALD process and film response windows for tantalum(V) ethoxide-derived Ta2O5
    ParameterPublished rangeFilm response if out of range
    Bubbler source temperature100 °C–140 °CCondensation or insufficient vapour delivery
    Substrate temperature250 °C–325 °CCarbon residue or degraded step coverage
    O3 pulse2 s–5 sIncomplete ethoxide oxidation
    Purge5 s–15 sGas-phase reaction and particle formation
    Post-anneal600 °C–700 °CIncomplete crystallization, leakage shift

    Thickness Uniformity Limits in Dip-Coated Ta₂O₅ Antireflective Stacks

    On ophthalmic BK7 glass, fused silica, and polycarbonate substrates, tantalum(V) ethoxide is converted into a hydrolyzed sol for dip-coated Ta2O5 layers in alternating high-low index interference stacks. A typical sol combines one molar equivalent of Ta(OEt)5 with glacial acetic acid and anhydrous 2-propanol, then receives controlled water addition to a final [H2O]/[Ta] ratio of 1.0–2.0. The acetic acid ligand slows hydrolysis and prevents immediate precipitation; the sol is filtered through 0.2 µm PTFE or polypropylene filters and aged for 30 min to 90 min before coating. Dip-coating withdrawal speeds between 1 mm/s and 3 mm/s produce single-layer thicknesses from 60 nm to 180 nm after drying; spin coating at 2,000 rpm to 4,000 rpm is used for planar substrates. Thermal curing at 400 °C to 500 °C in air removes organic residues and densifies the coating to a refractive index of 1.95 to 2.05 at 550 nm. On curved ophthalmic lenses, thickness variation across the surface is a stronger function of local solvent evaporation than withdrawal speed; a controlled solvent vapour pressure chamber with relative humidity below 40% is used to avoid edge-thickening. Adhesion is tested by cross-hatch method per ASTM D3359-17, with a 5B classification expected for properly cleaned glass; surface quality is inspected against MIL-PRF-13830B, and environmental durability follows ISO 9211-3 exposures to humidity, salt fog, and moderate abrasion. The hydrolyzed sol has a usable pot life of 8 h to 24 h depending on storage temperature; after that point, condensation produces gel particles that create optical scatter visible under dark-field inspection. In polycarbonate ophthalmic substrates, annealing is limited to 120 °C to 140 °C because higher temperatures distort the substrate, leaving a less densified Ta2O5 network with lower refractive index and reduced abrasion resistance. Process control therefore differs substantially between inorganic and polymeric lens production lines, and records from lens-coating operators identify airborne dust during dip withdrawal as the main cause of pinhole defects that fail ISO 9211-3 salt fog testing.

    Hybrid UV-curable formulations for LED encapsulants, image sensor microlenses, and nanoimprint lithography working stamps are prepared by dispersing Ta2O5 nanoparticles derived from tantalum(V) ethoxide into acrylate or methacrylate matrices. The ethoxide is first hydrolyzed in a two-phase ethanol-water system with methacryloxypropyltrimethoxysilane as a surface modifier, keeping the molar ratio of silane to tantalum at 0.3–1.0 to prevent agglomeration. After solvent exchange and distillation, dispersions with mean particle sizes below 20 nm by dynamic light scattering are blended at inorganic loadings up to 40 wt% to raise the cured refractive index at 589 nm from 1.48 to 1.68–1.78 while maintaining visible-light transmittance above 90% through a 50 µm film. Photoinitiated curing is performed with UV-LED sources at 365 nm or 385 nm and irradiance of 100–300 mW/cm²; the high metal oxide content reduces double-bond conversion, so longer post-exposure dark cure may be required. Adhesion to silicon nitride and glass passivation layers is evaluated by ASTM D3359-17, and thermal cycling stability follows JEDEC JESD22-A104 condition B for encapsulated devices. This application places strict limits on residual ethanol and hydrolysis by-products, because outgassing during UV cure can create microvoids at the encapsulant–chip interface.

    When Excess Lithium Acetate Is Added to a Ta(OEt)₅ Sol for SAW Substrates

    Lithium tantalate thin films for surface acoustic wave devices and pyroelectric sensors are deposited from a 2-methoxyethanol solution in which tantalum(V) ethoxide is co-reacted with lithium acetate. Lithium loss during high-temperature crystallization forces the initial Li:Ta molar ratio to be shifted to 1.05–1.15:1; without excess lithium, LiTa3O8 or lithium-deficient phases appear after annealing. Spin coating at 3,000–5,000 rpm on Pt/Ti/SiO2/Si substrates is followed by pyrolysis at 350 °C and final annealing at 650 °C to 750 °C in oxygen. The resulting film develops c-axis orientation only when the heating rate is controlled between 5 °C/min and 15 °C/min and the oxygen flow is sufficient to remove carbon residues before densification closes surface porosity. Film thickness per coating pass reaches 80–150 nm; repeated deposition and annealing cycles are needed for resonator-grade films above 500 nm. Process control is complicated by the moisture sensitivity of the ethoxide and the strong dependence of lithium distribution on platinum electrode roughness. Published data for this specific configuration is limited; most production SAW substrates are bulk LiTaO3 crystals, not thin films, so coatings derived from Ta(OEt)5 are typically restricted to research-scale resonators and sensor prototypes rather than volume manufacturing.

    In lithium-ion battery research, tantalum(V) ethoxide is applied as an ALD precursor for ultrathin Ta2O5 surface layers on nickel-rich NMC cathode powders. Rotary ALD reactors with continuous powder agitation and substrate temperatures between 180 °C and 250 °C are required because higher temperatures induce oxygen loss from the cathode lattice. Films of 1–3 nm thickness are deposited to reduce transition metal dissolution in carbonate electrolytes without blocking lithium transport. Electrochemical impedance spectroscopy on half-cells shows a modest increase in charge-transfer resistance at growth rates above 0.3 Å/cycle, so low-per-cycle deposition is favored. Published data for this specific configuration is limited; most reports use mixed alkylamide precursors rather than ethoxide, and tantalum ethoxide is adopted only when water-free delivery is required to avoid premature cathode surface hydroxylation.

    Tantalum(V) ethoxide has been evaluated for UV-only photocatalytic Ta2O5 films on quartz and glass reactor internals. The wide band gap of 4.0 eV limits excitation to sub-300 nm light, so low-pressure mercury sources at 254 nm are required; visible-light or UVA-LED systems do not generate sufficient electron-hole separation. Laboratory films deposited by dip coating and annealed at 500 °C show measurable stearic acid degradation under 254 nm irradiation, but reaction rates are consistently lower than those of anatase TiO2 control films. This application is not widely commercialized because the operating cost of short-wavelength UV and the lower quantum efficiency restrict practical deployment to specialized quartz sleeve photoreactors where titanium dioxide cannot be used due to side reactions.

    Does Hydrolysis Heat Release Destabilize Ethanol-Based Tantalum Sols in Humid Coating Hoods?

    Corrosion-resistant Ta2O5 coatings on 316L stainless steel and unalloyed titanium chemical process hardware are produced by dip coating from ethanol-based tantalum(V) ethoxide sols that have been partially hydrolyzed with controlled water additions. The exothermic hydrolysis reaction raises local solution temperature and, in ambient hoods above 45% relative humidity, accelerates condensation and precipitation; coating facilities therefore maintain humidity below 40% and jacket sol reservoirs to 18–22 °C. Coatings are fired at 450 °C to 550 °C under flowing nitrogen or argon, followed by a short air oxidation step, to form a conformal oxide layer with thickness 0.5–2 µm. Potentiodynamic polarization testing according to ASTM G5-14 in 30 wt% sulfuric acid at 80 °C shows reduced anodic current density compared with uncoated 316L, provided the film is free of pinholes and sub-surface cracks. Adhesion is checked by ASTM D3359-17; salt spray exposure under ISO 9227:2022 is used for quality release. The main incompatibility is with fluoride-containing process streams, because hydrofluoric acid etches Ta2O5 rapidly, and with concentrated phosphoric acid at elevated temperature, which extracts tantalum gradually. Equipment used for sol preparation must be dried and purged with inert gas, and residual ethanol in the film must be fully removed before annealing to avoid carbonization defects that reduce barrier performance.

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    Certification & Compliance
    More Introduction
    Tantalum(V) ethoxide (CAS 29156-11-0; linear formula Ta(OCH2CH3)5; molecular weight 406.25 g mol⁻¹) is supplied as a high-purity liquid alkoxide for deposition of tantalum-containing oxide films. Commercial model designations are not harmonized; a typical high-purity grade is identified as TaOEt-5N, indicating 99.999% metals-basis purity, while TaOEt-4N is specified at 99.99%. The material solidifies near 21°C and is therefore transferred after warming to 30–40°C. Density at 25°C is 1.566 g mL⁻¹, refractive index nD20 is 1.488, and reduced-pressure boiling is reported at 155°C under 0.1 mmHg. The ethoxide hydrolyzes rapidly in ambient air, generating ethanol and insoluble tantalum oxyhydroxide; handling is performed only under argon or nitrogen with moisture levels below 1 ppm. Tantalum mass fraction in the stoichiometric ethoxide is approximately 44.5%. Because coordinated ethanol and partial hydrolysis shift gravimetric recovery, certificates of analysis may report a Ta assay range of 44.2–45.0 wt% instead of a single theoretical value. The product is soluble in anhydrous ethanol, toluene, and hexane; contact with alcohols containing dissolved water or with non-inerted transfer lines results in ligand exchange or hydrolysis. Packaging interfaces are usually glass ampoules or electropolished stainless steel bubblers with metal gasket face-seal connections. Common fill sizes include 25 g, 100 g, 500 g, and 1.8 L. Filling is often conducted under nitrogen in an ISO 14644-1 Class 5 cleanroom to limit particle burden. The model code should be read together with the certificate of analysis because different suppliers use different purity suffixes; procurement specifications should state metal basis purity, niobium and chloride limits, water content, and packaging size.

    When Halide-Free Ta2O5 Deposition Replaces TaCl5 in Gate Stack Processing

    On production-scale ALD clusters, the selection of Ta(OEt)₅ rather than TaCl₅ is driven by the need to eliminate chloride from the film and from the reactor foreline. TaCl₅ releases HCl during hydrolysis; chloride residues can accelerate corrosion of stainless-steel exhaust lines and can become incorporated at the interface. Ta(OEt)₅ releases ethanol during oxidation, which is pumped away and does not generate acidic condensate. The resulting Ta2O5 films are deposited with H2O or O3 oxidant pulses at substrate temperatures typically set between 250°C and 350°C. Growth-per-cycle varies with precursor dose, residence time, and chamber geometry; published data for this specific configuration are limited, so baseline runs on the target tool are required before electrical qualification. The absence of chlorine does not remove moisture sensitivity—the precursor still hydrolyzes within seconds in humid air.

    Comparison of Tantalum(V) Ethoxide and Tantalum(V) Chloride
    Characteristic Tantalum(V) ethoxide Tantalum(V) chloride
    Hydrolysis byproduct Ethanol HCl
    Molecular weight 406.25 g mol⁻¹ 358.21 g mol⁻¹
    Ta mass fraction 44.5% 50.5%
    Melting behavior Solidifies near 21°C Melts near 216°C
    Chloride content <30 ppm in 5N grade Intrinsic chloride
    Reactor metal compatibility Lower acid-corroding potential Requires high-alloy or coated foreline
    Thermal stability in vapor phase Lower; carbon-bearing decomposition products possible Higher

    Purity Specifications, Trace Metals, and Analytical Certification for Ta(OEt)₅

    Certificates of analysis for 5N tantalum ethoxide typically report the following indicative ranges; lot-specific values must be verified against the supplier’s data because purification routes differ.

    Indicative specification ranges for Ta(OEt)₅ 5N grade
    Parameter Indicative range Analytical method
    Appearance Colorless to pale-yellow liquid Visual
    Ta metal basis purity 99.999% ICP-MS
    Ta assay 44.2–45.0 wt% Gravimetric oxide conversion
    Niobium (Nb) <50 ppm ICP-MS
    Iron (Fe) <15 ppm ICP-MS
    Chloride (Cl) <30 ppm Ion chromatography
    Water (H2O) <50 ppm ASTM E203
    Density at 25°C 1.566 g mL⁻¹ ASTM D4052
    Refractive index nD20 1.488 ASTM D1218
    Solidification point 21°C Differential scanning calorimetry

    Trace-metal limits are driven by dielectric leakage and interface stability. Niobium, iron, and chromium are measured by ICP-MS with matrix-matched calibration; chloride is determined by ion chromatography to detect residues from chloride-based purification. Water is determined by Karl Fischer titration under ASTM E203. Density and refractive index are used as rapid lot-release indicators; a density below 1.55 g mL⁻¹ may indicate ethanol dilution or hydrolysis. Solidification point is measured by differential scanning calorimetry because a depressed or broadened melt endotherm can indicate the presence of ethanol or ligand-exchange products. Batch-to-batch variation is most frequently observed in trace-metal levels when the source mineral feed changes; niobium and iron are the elements with widest variation. For that reason, some production lines require a qualification lot from each new ampoule and monitor liquid turbidity with a non-contact optical sensor before connecting to the process line.

    What Limits Liquid Delivery Repeatability in a Tantalum Ethoxide Bubbler System?

    Liquid delivery repeatability is controlled by solidification, moisture ingress, and thermal decomposition. Because the solidification point is near 21°C, a bubbler cabinet maintained at 20°C can produce a solid plug in the dip tube or reduce vapor draw. Jacket temperature should be maintained at 35–45°C; if the source is heated above 150°C for extended periods, decomposition residue accumulates in bellows seals and downstream valve seats. Moisture ingress through a leaking exhaust valve can hydrolyze the precursor in the headspace, increasing turbidity and raising pressure drop across the outlet frit. Source vessels with 0.5 µm or 0.2 µm sintered metal outlet filters should be monitored for filter differential pressure; an increase greater than 10 kPa during a single campaign is used in some facilities as a replacement criterion. Published data for this specific filter configuration are limited, but the failure mode is not gradual under high-humidity breach.

    Direct liquid injection systems dilute the alkoxide in anhydrous toluene or octane at 0.05–0.1 M. The solvent must be dried to below 50 ppm water before mixing. Liquid mass flow controllers must be calibrated for the blended solvent rather than for the neat precursor because viscosity and density differ. Point-of-use filtration at 0.1 µm PTFE is applied to remove precipitates that form slowly during long campaign runs. At ambient relative humidity above 60%, pre-drying of transfer syringes and anhydrous solvent is required before use. The precursor should not be mixed with amine-based additives prior to the intended hydrolysis step because basic catalysis accelerates gelation and can generate localized precipitate.

    In sol-gel processing, Ta(OEt)₅ is used to prepare Ta2O5 and mixed-oxide layers. A controlled hydrolysis ratio Rw = [H2O]/[Ta] is maintained between 2 and 8, with nitric acid used to adjust pH to 1–3. The sol is spin-coated or dip-coated and annealed at 650–750°C; the annealing atmosphere and heating rate influence crystallization and refractive index. For optical thin films, refractive index at 633 nm for annealed Ta2O5 is reported near 2.1, but ellipsometric values depend on porosity and dispersion model selection. Published data for this specific configuration are limited, so spectroscopic ellipsometry calibration is required for each substrate type. Compared with tantalum(V) isopropoxide, the ethoxide offers a lower molecular weight and generally higher vapor pressure at fixed source temperature; compared with tantalum(V) butoxide, it introduces less organic residue per metal center. These differences do not make the ethoxide more stable toward moisture. The ethoxide hydrolysis rate is faster than that of sterically hindered sec- or tert-alkoxides, so bubblers and glovebox interfaces using Ta(OEt)₅ require stricter headspace dryness. Metal-insulator-metal capacitor films deposited from Ta(OEt)₅ are evaluated with capacitance–voltage and current–voltage measurements on device-specific test structures; leakage and breakdown specifications are lot- and device-specific rather than fixed by the precursor supply.