Wet Electronic Acetonitrile G3 G5

Wet Electronic Acetonitrile (G3-G5)

    • Product Name: Wet Electronic Acetonitrile (G3-G5)
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 999572
    Product Name Wet Electronic Acetonitrile (G3-G5)
    Grade G3-G5
    Cas Number 75-05-8
    Molecular Formula C2H3N
    Molecular Weight 41.05 g/mol
    Physical State Liquid
    Appearance Clear, colorless liquid
    Odor Ether-like
    Purity ≥99.9% acetonitrile basis, grade-dependent
    Water Content Wet grade; grade-dependent
    Density 0.786 g/cm³ at 25 °C
    Boiling Point 81-82 °C
    Melting Point -45 °C
    Flash Point 2 °C (closed cup)
    Autoignition Temperature 524 °C
    Vapor Pressure 9.7 kPa at 20 °C
    Refractive Index 1.344 at 20 °C
    Viscosity 0.34 mPa·s at 25 °C
    Solubility Miscible with water and common organic solvents

    As an accredited Wet Electronic Acetonitrile (G3-G5) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Wet Electronic Acetonitrile (G3-G5) is supplied in 200 L nitrogen-purged stainless steel drums, sealed against moisture and contamination.
    Container Loading (20′ FCL) 20′ FCL loading of Wet Electronic Acetonitrile (G3–G5) in compliant drums, with secure stowage and hazardous chemical handling precautions.
    Shipping Wet Electronic Acetonitrile (G3-G5) ships as UN 1648, Acetonitrile, Class 3 flammable liquid, Packing Group II, in sealed high-purity containers. Transport away from ignition sources, oxidizers, and acids; keep containers closed and label per IMDG/IATA/ADR requirements.
    Storage Store in a cool, dry, well-ventilated, fire-resistant area away from ignition sources, heat, oxidizers, acids, and moisture. Keep containers tightly closed, labeled, and grounded; use compatible materials and secondary containment. Protect from sunlight and freezing. Maintain spill kits and inventory. Handle with local exhaust and, if needed, inert atmosphere to preserve electronic-grade purity.
    Shelf Life Shelf life is typically 12 months from date of manufacture when stored sealed in the original container under recommended conditions.
    Application of Wet Electronic Acetonitrile (G3-G5)

    In electric double-layer capacitor electrolyte preparation, wet electronic acetonitrile G3–G5 is charged into closed-loop blending skids fabricated from 316L electropolished stainless steel and passivated with dilute nitric acid. The solvent is dried through molecular sieve beds to a Karl Fischer moisture endpoint below 20 ppm before tetraethylammonium tetrafluoroborate is added to 1.0 mol/L. Conductivity of the finished electrolyte at 25 °C is controlled at 55 ± 2 mS/cm, while dynamic viscosity is retained at 0.34 mPa·s. Batch-to-batch conductivity drift on production lines is observed when post-drying water content exceeds 30 ppm, because residual moisture hydrolyzes BF4− and generates HF; the acid number is therefore held below 1 ppm HF equivalent by automatic titration. The electrolyte passes through 0.2 µm polypropylene cartridge filters and is vacuum-filled into wound or stacked cells under a dew point of −60 °C. Terminal products include 2.7 V EDLC cells and modules for wind-turbine pitch control, automotive start-stop systems, and industrial UPS. Cell-level qualification follows IEC 62391-1:2022 and IEC 62391-2:2022; solvent cleanliness is defined in SEMI C30-0611. Acetonitrile-based EDLC electrolytes are not used in cells with lithium or sodium metal anodes because of solvent reduction at the metal–electrolyte interface.

    Electrolyte property1.0 mol/L TEABF4 in acetonitrile1.0 mol/L TEABF4 in propylene carbonate
    Conductivity at 25 °C55 ± 2 mS/cm11 ± 1 mS/cm
    Dynamic viscosity at 25 °C0.34 mPa·s2.5 mPa·s
    Maximum operating voltage2.7 V2.7 V
    Karl Fischer moisture limit for electrolyte blending<20 ppm<30 ppm

    Why Does the I3−/I− Redox Couple in Dye-Sensitized Cells Demand Acetonitrile-Rich Solvents?

    The liquid redox electrolyte in dye-sensitized solar cells is formulated around a mixed solvent of acetonitrile and valeronitrile at 85:15 v/v. A representative electrolyte contains 0.1 mol/L lithium iodide, 0.6 mol/L 1,2-dimethyl-3-propylimidazolium iodide, 0.05 mol/L iodine, and 0.5 mol/L 4-tert-butylpyridine. Wet electronic acetonitrile G3–G5 is used to maintain iron, nickel, and copper impurities below 10 ppb because transition-metal contaminants accelerate iodide oxidation and increase dark current density at the photoanode. The electrolyte is backfilled under vacuum into the dye-sensitized TiO2 electrode gap through pre-drilled counter-electrode apertures at cell body temperatures from 35 °C to 50 °C. Pressure is restored to atmospheric level over 60 s to 120 s, and the aperture is sealed with a Surlyn gasket and cover glass. The atmospheric boiling point of acetonitrile, 81.6 °C, constrains thermal sealing steps; sealing is therefore performed before electrolyte injection or at reduced temperature. Terminal products are indoor photovoltaic modules, portable solar chargers, and low-light energy-harvesting panels. Module-level reliability testing follows IEC 61646:2008, and current–voltage verification is conducted under IEC 60904-1:2020. Density of the finished electrolyte at 25 °C is controlled at 0.78 g/cm³, and moisture exposure above 50 ppm during filling is known on pilot lines to increase charge-transfer resistance at the counter electrode.

    Single-wafer processors dedicated to post-etch residue removal use heated acetonitrile at 40 °C to 60 °C as a polar aprotic rinse for organic etch by-products on patterned wafers without attacking aluminum or copper interconnects. Where drying rate and flammability require adjustment, acetonitrile is blended with isopropanol at 70:30 to 90:10 v/v, and the blend is recirculated through 0.05 µm PTFE point-of-use filters before being dispensed through a low-flow spray bar at 0.5 L/min to 1.5 L/min. Cleaning execution occurs in an ISO Class 5 minienvironment under ISO 14644-1:2015, and post-cleaning surface residue is verified by laser particle scanning combined with ion chromatography of wafer-extract solutions. The relevant solvent-level cleanliness specification is SEMI C30-0611 for trace metal and particle content. Terminal products from this operation are patterned wafers, photomasks, and flat-panel-display substrates entering subsequent lithography, deposition, or bonding steps. The closed-cup flash point of acetonitrile is 2 °C, so dispensing cabinets on production lines are classed for flammable liquid handling and are typically inerted with nitrogen. Acetonitrile is incompatible with strong oxidizers such as sulfuric acid–peroxide mixtures; dedicated waste segregation is mandatory. Published data for exact residue removal rates on specific photoresist families is limited, and process qualification for each device manufacturer is established through fall-on-wafer defect density testing.

    Perovskite Precursor Solvent Windows and Antisolvent Quench Behaviour

    Slot-die coating lines for perovskite photovoltaic absorbers use wet electronic acetonitrile G3–G5 either as a low-boiling co-solvent in precursor inks or as a quench solvent during film crystallization. When applied as a co-solvent, addition levels from 5 vol% to 20 vol% relative to dimethylformamide and dimethyl sulfoxide blends reduce solution viscosity and accelerate evaporation during slot-die or blade coating. As an antisolvent, the material is dispensed at 0.5 mL/cm² to 2.0 mL/cm² onto the wet precursor film, where it lowers solute solubility and triggers perovskite nucleation. The vapor pressure of acetonitrile at 20 °C is 9.7 kPa, which supports rapid removal after the quench step. G3–G5 metal contaminant limits are critical because transition-metal impurities in the parts-per-billion range act as non-radiative recombination centers in the absorber layer and reduce open-circuit voltage. Coating tools are equipped with 0.2 µm inline filters, and the wet film is thermally annealed at 100 °C to 140 °C after quench application. Terminal products are rigid and flexible perovskite solar modules. Cell-level current–voltage measurements follow IEC 60904-1:2020, and adapted module qualification is evaluated under IEC 61215-1:2021 where applicable. No dedicated perovskite module standard is currently published; correlated process windows are therefore derived from design-of-experiment matrices rather than fixed normative limits. Published data for exact antisolvent volumes across all perovskite chemistries is limited, so the quench ratio is optimized against film brightness, grain size, and photoluminescence intensity on the coating line.

    When Acetonitrile Replaces Carbonate Cosolvents in Electrochromic Electrolyte Formulations

    Electrochromic window laminators fill glass cavities with lithium-ion conducting electrolytes containing 0.1 mol/L to 0.5 mol/L lithium bis(trifluoromethanesulfonyl)imide in a solvent system of acetonitrile and propylene carbonate at 50:50 to 80:20 v/v. Wet electronic acetonitrile G3–G5 is selected for this use because its low viscosity, 0.34 mPa·s at 25 °C, facilitates rapid vacuum injection into narrow glass-cell gaps; the water content of the finished electrolyte is maintained below 20 ppm by Karl Fischer monitoring to avoid LiTFSI hydrolysis and tungsten oxide electrode degradation. Electrolyte injection is performed at 10⁻² mbar in a vacuum laminator, followed by edge sealing with a low-shrinkage epoxy or frit. After sealing, cells undergo electrochemical conditioning by cycling between −1.0 V and +1.0 V to stabilize coloration efficiency. Terminal products include electrochromic smart windows, dimmable automotive mirrors, and aircraft cabin window inserts. Accelerated durability testing follows ASTM E2141-06 for electrochromic device aging, with visible transmittance change and switching speed recorded at defined cycle counts. Production lines using acetonitrile-rich electrolytes must limit cavity temperature during seal curing because acetonitrile has a boiling point of 81.6 °C; therefore, edge sealing is conducted before injection or with low-temperature seal formulations. The solvent system is not compatible with water-containing hydrogel electrolytes or with unprotected lithium-metal electrochromic counter electrodes, where acetonitrile reduction generates decomposition products.

    Reverse-Phase HPLC Mobile Phases for OLED Material Release and Electronic Chemical Certification

    Mobile-phase preparation for high-performance liquid chromatography in OLED material supplier laboratories represents a downstream use of wet electronic acetonitrile G3–G5 in organic semiconductor purity assessment. Reverse-phase methods for non-polar host and transport compounds operate with acetonitrile–water gradients from 40 vol% to 95 vol% acetonitrile over 10 min to 15 min at 1.0 mL/min on a C18 column packed with 1.7 µm to 3.0 µm particles. For acidic or basic impurity classes, 0.1 vol% trifluoroacetic acid or formic acid is added to the aqueous component to suppress peak tailing. The acetonitrile must meet ultraviolet transmittance and LC-MS compatibility requirements, with specified minimum transmittance at 254 nm and low nonvolatile residue limits checked by evaporation after each solvent lot. Column temperature is held at 40 °C, and detection is performed by diode-array ultraviolet absorbance or quadrupole mass spectrometry depending on impurity targets. The production process for OLED material release therefore includes dissolution of the organic semiconductor sample in acetonitrile, gradient elution, integration of impurity areas against response factors, and reporting of total purity. Terminal products are purified OLED host materials, hole-transport materials, and electron-transport materials subsequently deposited into display device stacks. Analytical method validation follows ICH Q2(R1) for specificity, linearity, and repeatability; chromatographic system suitability is governed by USP General Chapter <621>. Acetonitrile-based reversed-phase methods are not suitable for normal-phase preparative separations of highly non-polar OLED intermediates that require heptane–ethyl acetate mobile phases.

    Free Quote

    Competitive Wet Electronic Acetonitrile (G3-G5) prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618005193850

    Email: sales8@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

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

    Certification & Compliance
    More Introduction

    Wet Electronic Acetonitrile (G3–G5) is a liquid polar aprotic solvent with CAS 75-05-8 and molecular formula CH3CN. The product is not anhydrous; the term “wet” designates a controlled-moisture liquid form rather than a zero-water product. The G3, G4, and G5 grade designations are lot-release categories that differ principally in water mass fraction, nonvolatile residue, trace metal burden, anion content, and submicrometer particle count. Electronic-grade acetonitrile of this class is distinguished from HPLC-grade, ACS, or pesticide residue analysis material by the addition of particle counting by laser light obscuration and trace-metal quantification by ICP-MS on each lot, and by packaging in cleaned fluoropolymer-lined or high-density polyethylene containers under nitrogen headspace. The solvent has a viscosity of 0.34 mPa·s at 25 °C and a closed-cup flash point near 2 °C as measured by ASTM D56, which places it in flammable liquid handling classifications. Packaging configurations commonly include 1 L, 4 L, and 20 L containers for manual dispense, with 200 L drums or stainless steel totes for facility fill lines. Because the material is hygroscopic, water content must be verified after any container has been opened outside a dry-room or nitrogen-purged dispense enclosure.

    Material Specification and Incoming Inspection Window

    Incoming inspection for wet electronic acetonitrile is typically configured around four analytical families: gas chromatography for assay and organic impurities, Karl Fischer coulometry for water, ICP-MS for trace cations, and light obscuration for particles. The values in the table below are representative of supplier lot-release data for G3–G5 material; they are not universal product specifications and should be read against the certificate of analysis for each lot. For semiconductor-grade acetonitrile, the analytical approach parallels SEMI C30-class methods. Assay is reported as area percent by GC-FID with internal normalization; water is determined by Karl Fischer titration according to ASTM E203; particle counts are obtained at 0.5 µm sensitivity using a laser particle counter calibrated with polystyrene latex spheres according to ISO 21501-3. Nonvolatile residue is measured by evaporation at 105 °C in tared platinum or quartz vessels. Trace metal totals are the sum of Li, Na, K, Mg, Ca, Fe, Cu, and Zn by ICP-MS; other transition-metal limits may be lot-specific.

    ParameterG3G4G5
    Assay, GC-FID area%≥99.90%≥99.99%≥99.999%
    Water, Karl Fischer ASTM E203≤100 ppm≤50 ppm≤20 ppm
    Nonvolatile residue, 105 °C≤5 ppm≤2 ppm≤1 ppm
    Trace metal sum by ICP-MS≤50 ppb≤20 ppb≤5 ppb
    Chloride by ion chromatography≤0.5 ppm≤0.2 ppm≤0.05 ppm
    Particles ≥0.5 µm, light obscuration≤50 particles/mL≤25 particles/mL≤10 particles/mL

    How Does G4 Wet Acetonitrile Perform as a Wash Solvent in Lithium Battery Electrolyte Filling Lines?

    In lithium-ion cell assembly, electrolyte filling nozzles and positive-displacement metering valves are rinsed with acetonitrile after exposure to LiPF₆-carbonate electrolytes. G4 is commonly selected for this duty because water mass fraction above 50 ppm in the cleaning solvent can transfer to residual film on stainless steel surfaces and hydrolyze LiPF₆ to HF and POF₃. The failure mode observed on production lines is not a bulk reaction but a slow increase in needle-tip particulates and iron release from 316L stainless steel contact surfaces. Rinsing with G4 material reduces the water-loading contribution to the hydrolysis sequence, but it does not eliminate fluoride generation if the wetted surface already contains acidic residues from prior electrolyte exposure. The cleaning performance depends on the nozzle geometry: narrow-gauge fill needles with internal diameter below 0.5 mm show greater sensitivity to particle release because capillary residues are not fully displaced by laminar rinse flow. In automated battery lines, recirculated acetonitrile rinse loops are filtered through 0.05 µm PTFE capsules; pressure drop across the filter capsule is monitored, and an increase of more than 0.2 bar over baseline often correlates with particle accumulation rather than viscosity shift. For cells with low electrolyte volume and low-tolerance moisture budgets, G5 material with water mass fraction at or below 20 ppm may be substituted; published data for this specific configuration is limited, but process control narrows because the cleaning solvent is a direct contact residual source.

    On display fabrication lines where fine metal mask cleaning is performed with polar aprotic solvents, G5 wet acetonitrile is applied as the final rinse after solvent stripping of organic light-emitting materials. The process operates at room temperature in an ultrasonic bath or in a single-wafer spin rinse module with point-of-use filtration. In this application, the difference between G4 and G5 is primarily particulate: shadow mask apertures with dimensions below 10 µm require particle levels below 10 particles/mL at 0.5 µm to avoid redeposition of silicon, aluminum, or stainless steel fragments on the mask edge. The product is used as a rinse rather than a bulk stripper because its Hansen solubility parameters provide effective dissolution for certain oligomeric residues but slower bulk removal than chlorinated solvents or blended NMP-based formulations. Production-scale experience shows that ultrasonic cavitation in acetonitrile can generate local temperature rise; the bath temperature is controlled at 25 °C ± 2 °C to prevent evaporation loss and water uptake. If the mask is transferred through an air curtain, water uptake at the container surface is limited by keeping the headspace under clean dry air or nitrogen; open-bath use beyond 8 h typically requires Karl Fischer re-verification.

    In Sub-10 nm Technology Nodes, Trace Cation Rejection Controls Final Watermark Density

    G5-grade wet acetonitrile is used in analytical extraction and rinse compatibility checks because background cation levels in the solvent must not exceed the surface metal budget of the wafer. A single wafer surface extraction sample using 20 mL of G5 material with a metal sum of 5 ppb contributes at most 100 ng of total specified metals if the entire extraction volume were deposited; real deposition efficiency is lower, but the solvent blank must remain below the detection limit of the subsequent ICP-MS measurement. In sub-10 nm technology nodes, wafer surface preparation specifications for certain mobile ions are stated at 1 × 10^10 atoms/cm² or lower; the extraction solvent therefore must have individual metal concentrations below 1 ppb for Na, Al, and Fe. G5 material is specified as sum ≤5 ppb, but lot-specific verification of each critical metal is necessary because a bulk sum can conceal an excursion in a single element. Particle requirements are similarly tight: any particle ≥0.2 µm that deposits on a patterned wafer can create a mask defect or block a subsequent atomic layer deposition step. Routine monitoring uses a scanning mobility particle sizer or liquid particle counter with 0.2 µm sensitivity; G5 material is commonly expected to have fewer than 10 particles/mL at this lower size threshold. The solvent must not be used to clean wafers with exposed alkali-sensitive films without compatibility testing; acetonitrile can swell or extract certain organic planarization layers and photoresist adhesion promoters.

    During development of photoresist strip and post-etch residue cleaners, wet electronic acetonitrile is employed as a carrier solvent for liquid chromatography–mass spectrometry of organic residues extracted from wafer surfaces. In this setting, the G3–G5 grade split controls background noise: G3 material with nonvolatile residue up to 5 ppm can produce a detectable unresolved landscape in total ion current when analyzing trace residue levels below 1 ng/cm². G5 material reduces the nonvolatile residue contribution and is preferred for method validation. The difference from HPLC-grade solvent is trace metal and particle control, not necessarily chromatographic absorbance; HPLC-grade acetonitrile may have suitable UV cut-off properties but lacks the particle and cation documentation required for wafer-level contamination studies. Because acetonitrile is miscible with water, it is also used to dilute aqueous process baths before ion chromatography; the chloride blank must be below 0.05 ppm for accurate quantification of chloride at 0.1 ppm in the diluted bath sample.

    When Acetonitrile Replaces NMP in Low-Moisture Polymer Dispersion

    Wet electronic acetonitrile is evaluated as a lower-boiling alternative to N-methyl-2-pyrrolidone in selected polymer dispersion and cleaning operations where the polymer is soluble in a polar aprotic medium. The comparison is limited by the solubility window: acetonitrile dissolves a narrower set of fluorinated and polar resins than NMP, and its fast evaporation can increase the risk of drying-induced surface defects in slot-die coating. In a flat-sheet coating trial on a roll-to-roll line with 0.3 m/min line speed and 120 °C dryer set point, batch-to-batch water variation in G3 material produced greater viscosity drift than G4 or G5; the practical control was to restrict the coating formulation to G4-grade material with water mass fraction ≤50 ppm and to pre-dry the polymer before dissolution. The evaporation rate of acetonitrile is higher than that of NMP, which reduces dryer energy demand but raises the lower explosive limit management burden near the coating head. Acetonitrile is not a direct substitute for NMP in most PVDF-based electrode coatings because PVDF solubility is limited in acetonitrile at room temperature; operator verification using a solubility screen at 10 wt% solids is required before production trials. Compared with anhydrous acetonitrile, the wet G3–G5 product offers a defined moisture window rather than an aggressively dried material; this is useful when the downstream process requires water as a kinetic control agent, such as in certain sol-gel reactions or where trace water prevents static charge accumulation. Compared with isopropanol and acetone, acetonitrile provides higher polarity and different residue solubility, but it also carries nitrile-specific incompatibilities: contact with strong oxidizers or strong aqueous acid at elevated temperature can generate cyanide species, and contact with strong bases can produce ammonia via hydrolysis. Storage should be isolated from oxidizing agents and from concentrated sulfuric acid; containers should be grounded during transfer because the solvent has conductivity below 100 pS/m unless a static dissipative additive is present.

    Top