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Silicon Tetrafluoride (SiF₄) Electronic/EL Grade

    • Product Name: Silicon Tetrafluoride (SiF₄) Electronic/EL Grade
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 251580
    Chemical Formula SiF4
    Molecular Weight 104.08 g/mol
    Cas Number 7783-61-1
    Grade Electronic/EL Grade
    Purity ≥99.999%
    Physical State At 20c And 1atm Gas
    Appearance Colorless gas
    Odor Pungent, suffocating
    Melting Point -90.2 °C
    Boiling Point -86.0 °C
    Density Gas At Stp 4.65 g/L
    Relative Vapor Density 3.59 (air = 1)
    Solubility Behavior In Water Reacts via hydrolysis, forming HF and silica/silicofluoride species
    Flammability Non-flammable

    As an accredited Silicon Tetrafluoride (SiF₄) Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in sealed high-pressure stainless steel cylinders, Silicon Tetrafluoride (SiF₄) Electronic/EL Grade, quantity 50 kg, ensuring purity and safe handling.
    Container Loading (20′ FCL) 20' FCL: ISO tanks or cylinders of high-purity SiF₄ securely stowed, segregated, and hazard-compliant for safe transport.
    Shipping Ship Silicon Tetrafluoride (SiF₄) Electronic/EL Grade as a liquefied compressed gas in dedicated, clean, high-pressure cylinders. Ensure DOT/UN approval, secure upright transport in ventilated vehicles, and use inert connections to prevent moisture contamination. Follow hazardous material regulations, proper labeling, and emergency response protocols.
    Storage Store Silicon Tetrafluoride (SiF₄), electronic/EL grade, as a compressed gas in certified, leak-tight steel or alloy cylinders. Keep cylinders upright, secured, and valved in a cool, dry, well-ventilated area. Isolate from moisture and incompatible materials. Use corrosion-resistant connections, proper labeling, and continuous leak monitoring. Ensure emergency scrubbers and appropriate PPE are available.
    Shelf Life Shelf life is typically 24 months when stored properly in a sealed cylinder, protected from moisture and heat.
    Application of Silicon Tetrafluoride (SiF₄) Electronic/EL Grade

    What Process Window Governs SiOF Deposition in Dual-Damascene Interconnects?

    In 300 mm logic and DRAM fabrication sequences, electronic-grade SiF4 is introduced into parallel-plate capacitively coupled plasma-enhanced chemical vapor deposition chambers as the fluorine donor for fluorosilicate glass, the low-dielectric intermetal dielectric that replaced undoped silicate glass at nodes where interconnect RC delay became the dominant speed limiter. The precursor stream is metered through dual-zone showerheads with SiF4:SiH4 volumetric ratios held between 1.0:1 and 3.0:1, while N2O oxidant flow is maintained at 2030 times the combined silane and SiF4 flow. Helium dilution of 6080 vol% stabilizes the discharge, total chamber pressure is controlled at 2.54.0 Torr, substrate temperature is held at 350400 °C, and RF power density at 13.56 MHz is set between 0.30 and 0.85 W cm−2. Under these production conditions, fluorine incorporation measured by X-ray photoelectron spectroscopy after argon sputter clean reaches 3.07.0 atomic percent, reducing the dielectric constant from 4.1 for undoped SiO2 to 3.53.7 at 1 MHz mercury-probe C-V measurement. Compliance for the deposition module and gas delivery follows SEMI C3.51 for electronic-grade SiF4 specifications, SEMI S2-0200 equipment safety parameters, ISO 14644-1:2015 Class 3 cleanroom protocols for gas manifold installation, and the IRDS interconnect roadmap constraints for allowable dielectric k-value drift after thermal stress. The delivery line is fabricated from electropolished 316L stainless steel with 10 Ra microinch internal finish, and the moisture specification at the point of connection is held below 10 ppb(v) to suppress premature hydrolysis of SiF4 to SiO2 particulates and HF.

    SiF4/(SiH4+SiF4) volumetric ratioRF power density (W cm−2)Fluorine content (at%)Dielectric constant at 1 MHzWet etch rate ratio in 0.5 wt% HF
    0.300.653.23.651.6
    0.450.754.83.552.1
    0.600.856.73.482.8

    The downstream integration sequence for FSG uses a dual-damascene copper/low-k flow: after FSG deposition on a 300 mm PECVD platform with electrostatic chuck temperature uniformity of ±3 °C, a 2050 nm undoped SiO2 liner is deposited to suppress fluorine scavenging by the subsequent Ti/TiN barrier, followed by copper seed, electrochemical plating, and chemical mechanical planarization. Thermal exposure after FSG deposition is confined to 400 °C for 30 min or less because dissociative loss of silicon-bound fluorine above 450 °C liberates HF at the FSG-barrier interface, increases film stress, and raises k-value by 0.10.2. Wet etch rate in 0.5 wt% hydrofluoric acid increases by a factor of 1.62.8 relative to undoped oxide, which requires endpoint tuning in via etch and photo-resist strip to avoid critical dimension blowout. Terminal product types include application processors, DRAM stacked-capacitor interconnect dielectrics, embedded non-volatile memory devices, and high-performance logic SoCs fabricated from 90 nm down to 45 nm design rules. Exposed FSG surfaces must be queued under nitrogen or vacuum if wafer delay exceeds 4 h because ambient moisture adsorption raises the effective dielectric constant and generates silanol groups observable by FTIR at 34003600 cm−1.

    In single-mode optical fiber preform manufacturing, SiF4 functions as the fluorine donor for depressed-cladding refractive-index profiles rather than as a silicon precursor. For modified chemical vapor deposition and plasma chemical vapor deposition processes, the vapor-phase SiF4 concentration is controlled between 0.5 and 2.5 mol% of total silicon precursor, with typical PCVD gas flows for a 25 mm internal diameter silica substrate tube set at 50200 sccm SiF4, 100300 sccm SiCl4, and 1.02.0 slm O2 at 1015 mbar. The resulting fluorine content of 1.03.0 wt% in consolidated cladding glass produces a relative refractive index reduction δn/n of −0.20% to −0.50%, sufficient to form bend-insensitive and depressed-cladding waveguides while maintaining viscosity compatibility across the core-cladding interface. Compliance at the fiber level is anchored to IEC 60793-2-50:2018 for class B single-mode fiber specifications, ITU-T G.652.D for zero water peak transmission, ITU-T G.657.A2 for reduced bend radius, and ANSI/TIA-492 family performance requirements. In PCVD, the deposition occurs at 11001300 °C inside the tube by low-pressure non-isothermal plasma activation, after which the preform is consolidated at 14001500 °C in a graphite resistance furnace under a chlorine or SiF4 atmosphere to remove hydroxyl species and densify the glass to bubble-free state. In outside vapor deposition, soot is deposited on a rotating bait rod and later consolidated in He/SiF4 at similar sintering temperatures, with fluorine incorporation occurring during the pore-closure phase rather than during initial particle formation. The vapor delivery skid requires sealed bubblers for SiCl4 and high-purity mass flow controllers for SiF4; exhaust gas carries unreacted SiF4 and HF, demanding packed-bed caustic scrubbers with pH monitoring and fluoride-specific sensors. Terminal product types include long-haul DWDM fibers, reduced-bend-radius access fibers specified to G.657.A2, zero water peak fibers, and polarization-maintaining fibers for fiber-optic gyroscopes and distributed acoustic sensing. The critical operational boundary is moisture exclusion: SiF4 hydrolyzes to silica dust and HF if the carrier gas dew point exceeds −70 °C, causing mass flow controller drift and requiring line purging with dry nitrogen for 24 h after any maintenance event.

    Fluorine-Doped Synthetic Fused Silica for 193 nm DUV Lithography Components

    SiF4 is delivered to oxy-hydrogen flame hydrolysis burners at 0.51.5 slm as the fluorinating dopant for synthetic fused silica boules used in deep-ultraviolet projection optics, while a silicon precursor such as SiCl4 or an organosilane is fed at 0.31.0 slm. Fluorine content in the consolidated glass is maintained at 0.52.0 wt%, producing a refractive index reduction of 0.10.3% relative to undoped fused silica and suppressing laser-induced densification under 193 nm irradiation at fluences above 1 mJ cm−2 per pulse. The vitrification step occurs at 16001800 °C on a rotating fused silica bait ingot, followed by homogenization annealing at 11001200 °C for 1030 days to reduce thermal history-induced birefringence. Surface and bulk compliance is specified by ISO 10110-7:2017 for surface imperfections, ISO 10110-14:2018 for wavefront deformation, and SEMI S2-0200 for equipment safety; DUV transmission uniformity is verified periodically by excimer-laser calorimetry and spectrophotometric scans in the 190300 nm range. On the production floor, the multi-axis burner lathe uses electronic mass flow control with upstream pressure regulation to hold fluorine distribution within ±0.1 wt% across a 300 mm diameter boule cross-section. The combustion process generates HF as a reaction byproduct, requiring wet scrubbing of exhaust gas and continuous downstream fluoride monitoring. Terminal product types include projection lens elements for 193 nm immersion and dry scanners, excimer laser resonator optics, photomask substrates, and DUV metrology reference windows. The operational boundary for raw material handling is strict: if SiF4 delivery lines contain hydrocarbon or siloxane residues, flame combustion generates carbonaceous inclusions that raise absorption at 193 nm, so stainless-steel lines are vacuum-baked at 120 °C for 8 h before first flow.

    For plasma-assisted fluoride thin-film growth on DUV-grade optical substrates, SiF4 is introduced as the fluorinating co-reactant in atomic layer deposition sequences using capacitively coupled RF plasma excitation at 13.56 MHz. The metal precursor, typically trimethylaluminum or bis(cyclopentadienyl)magnesium depending on the target metal fluoride, is pulsed for 0.10.5 s, followed by purge of 520 s, then SiF4 pulse of 0.21.0 s at 20100 sccm. Substrate temperature is maintained between 150 and 250 °C, yielding a growth rate of 0.41.0 Å per cycle for optically smooth fluoride films. The process is conducted in a warm-wall ALD chamber with in-situ ellipsometry viewing ports; excessive plasma power above 300 W causes silicon incorporation into the growing fluoride layer and shifts refractive index by more than 0.02 at 633 nm, which is outside the tolerance for quarter-wave DUV stack designs. Compliance for coated components is checked against ISO 9211-1:2018 for optical coatings and MIL-PRF-13830B surface quality criteria where defense-grade DUV optics are involved. Published data for this specific high-volume production configuration is limited, and the process window remains sensitive to chamber seasoning history and residual water vapor. The deposition system must avoid moisture ingress above 5 ppm(v) in the load lock because SiF4 rapidly hydrolyzes to silica particles and HF, generating chamber defects that reduce laser damage threshold below the 1 J cm−2 acceptance level for excimer-laser coatings. Terminal product types include DUV antireflective coatings, thin-film polarizers, high-reflectivity mirrors for excimer laser beam delivery, and beamsplitter coatings for 248 nm and 193 nm optical systems.

    SiF4 Calibration Mixtures Support Semiconductor Exhaust Monitoring

    Electronic-grade SiF4 is gravimetrically blended into passivated aluminum cylinders at concentrations between 5 and 100 ppmv in nitrogen or helium balance to generate Fourier transform infrared and quadrupole mass spectrometer calibration standards for semiconductor exhaust monitoring. High-concentration reference mixtures of 12 vol% SiF4 are used for method linearity verification on continuous emission monitoring systems installed downstream of etch clean processes. Cylinder preparation follows ISO 6142-1:2015 gravimetric methods and ISO 6143:2001 comparison validation, with internal cylinder surfaces treated with fluoropolymer passivation to reduce SiF4 adsorption and hydrolysis. The filling sequence uses a two-stage evacuation to below 10−6 mbar, followed by gravimetric addition of SiF4, balance gas addition, and roll-mill homogenization at 40 °C for 24 h. Stability verification is performed by gas chromatography with thermal conductivity detection and FTIR at 1030 cm−1 for the Si–F stretching band. Terminal product types include primary calibration gas cylinders for fabrication plant exhaust analytics, residual gas analyzer calibration cells, scrubber efficiency validation kits, and process tool leak detection standards. Operational boundaries are defined by the reactive behavior of SiF4 in moist environments: cylinders must be dried to a dew point below −60 °C before filling, regulators are restricted to stainless-steel or Monel construction, and shelf life is limited to 12 months from certification when stored at 20 °C to 25 °C.

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    Certification & Compliance
    More Introduction

    As a silicon-halide source, Silicon Tetrafluoride (SiF₄) Electronic/EL Grade is supplied as a compressed gas in electropolished 316L stainless steel cylinders under supplier designations such as SiF₄-EL-4N, SiF₄-EL-5N, and SiF₄-EL-6N. The product is registered under REACH EC 232-015-5 and shipped under UN 1859. Its molar mass is 104.08 g/mol, gas density is approximately 3.6 relative to air, and normal boiling point is -86 °C. The Electronic/EL grade differs from industrial SiF₄ by controlled levels of transition metals, moisture, total acid, and particulates. These impurities are process-critical: metallic contamination above 10 ppbw shifts flatband voltage in metal-oxide-semiconductor structures, while moisture above 1 ppmv promotes hydrolysis to hydrogen fluoride and silica particles in gas delivery lines. Supplier lot certificates for 99.999 vol% material therefore list assay, oxygen, nitrogen, carbon dioxide, total acids as hydrogen fluoride, total metals, and particle load. Gas analysis is typically performed by gas chromatography with pulsed-discharge helium ionization detection, Fourier-transform infrared spectroscopy according to ASTM D6348-12, and cavity ring-down spectroscopy calibrated with gravimetric gas standards prepared according to ISO 6142-1.

    How Electronic/EL Grade SiF₄ Is Distinguished from Industrial-Grade Material

    Before procurement, the packaging and purity definitions of Electronic/EL SiF₄ should be compared directly against supplier lot limits because no universal SEMI specification for SiF₄ grade nomenclature exists across all manufacturers. Industrial-grade SiF₄ used in glass etching or cement processing may contain hydrogen fluoride and water at levels orders of magnitude above electronic requirements. The Electronic/EL grade does not simply raise the silicon tetrafluoride assay; it controls minority species that govern dielectric response, optical transmission, and surface morphology in downstream films. Table 1 provides a representative supplier lot acceptance profile for 5N material. Limits vary by manufacturer and should be confirmed against the actual certificate of analysis before qualification.

    Table 1. Representative supplier lot acceptance profile for SiF₄ Electronic/EL 5N
    ParameterAcceptance LimitTypical Analytical Method
    Assay99.999 vol%Gas chromatography with pulsed-discharge helium ionization detector
    H₂O1 ppmvCavity ring-down spectroscopy
    O₂5 ppmvGC-PDHID
    N₂10 ppmvGC-PDHID
    CO₂5 ppmvGC-PDHID
    Total acids as HF10 ppmvIon chromatography after impinger collection
    Total metals10 ppbwInductively coupled plasma mass spectrometry following hydrolytic collection
    Particles ≥ 0.1 µm3 particles/scfLaser particle counter in an ISO 14644-1:2015 Class 5 environment

    Across 200 mm and 300 mm manufacturing lines, the relevant difference between Electronic/EL products and other high-purity SiF₄ grades often resides in detection limits, not in the chemical identity of the gas. A front-end gate oxide process may require total metals below 1 ppbw, while an interconnect dielectric application may tolerate 10 ppbw. Published data for this specific configuration is limited; qualification therefore proceeds by lot-by-lot analysis using hydrolytic impinger collection followed by ISO 17294-2 measurement. Moisture and acid limits are equally critical because SiF₄ hydrolyzes rapidly to form hydrogen fluoride and nonvolatile silica. That hydrolysis pathway means that a cylinder with acceptable assay can still fail downstream if moisture ingress occurs during changeout or in the gas manifold.

    Vapor Delivery and Cylinder Conditioning Requirements

    During cylinder changeout, a purge-assisted valve manifold is required to exclude atmospheric moisture. Gas cabinets should feed SiF₄ through a pressure regulator and mass flow controller calibrated for SiF₄ because silica formed by hydrolysis can accumulate on downstream surfaces and alter flow calibration. In production installations, delivery lines are constructed from electropolished 316L stainless steel tubing with mechanical surface roughness below 0.25 µm Ra and joined by orbital welding. Helium leak testing of the assembled manifold is specified at no greater than 1 × 10⁻⁹ Pa·m³/s to prevent ingress. Cylinder storage follows CGA P-1 compressed gas handling requirements, including temperature limits below 52 °C and separation from water, ammonia, amines, and alkali metal hydroxides. At relative humidity above 60%, purge cycles are extended because adsorbed water on internal surfaces converts SiF₄ to HF and silica. Point-of-use purifiers with 0.003 µm particulate filtration are installed upstream of the mass flow controller to capture silica particles released during pressure cycling. Valve outlets should be protected by dry nitrogen purge when disconnected, and cylinder changeout should follow the supplier evacuation procedure because residual SiF₄ exposed to humid air can generate solid silica in the valve seat.

    For interlayer dielectric deposition, SiF₄ is metered into high-density plasma chemical vapor deposition chambers through mass flow controllers at flow rates typically between 5 and 50 sccm for a 200 mm wafer tool. Chamber pressure is held in the 2–8 Torr range, and RF power density is adjusted between 0.5 and 2.0 W/cm². Co-flow of silane and oxygen converts the mixture to fluorinated silicate glass. Published studies report that fluorine incorporation of 3–6 at% lowers dielectric constant from approximately 4.0 to 3.4–3.5, reducing line-to-line capacitance in damascene interconnects. FTIR spectra of the film show the Si-F stretching band near 940 cm⁻¹; the intensity ratio of this band to the Si-O-Si absorption is used as an inline metric for fluorine dose. At fluorine levels above 8 at%, films become porous and moisture-sensitive, increasing leakage current and requiring post-deposition stabilization. Production observations indicate that excessive F/Si precursor ratios shift the deposition regime toward gas-phase nucleation instead of surface reaction; the resulting particulates accumulate on the showerhead and require more frequent in situ cleaning with NF₃-based processes.

    In optical fiber preform manufacturing, SiF₄ is used during modified chemical vapor deposition as the fluorine precursor for cladding index depression. The gas is injected with oxygen and silicon tetrachloride into the rotating substrate tube. Fluorine substitutes for oxygen in the silica network and lowers the refractive index by approximately 0.1–0.3% relative to undoped silica, depending on flow ratio and deposition temperature. The absence of hydrogen in the SiF₄ molecule avoids hydroxyl absorption near 1.38 µm, which is a limitation of hydrogen-containing fluorine dopants. Equipment-level data show that exhaust line blockages from silica formation occur more frequently when SiF₄ is introduced downstream of unheated sections, because the hydrolysis rate is temperature-dependent. Published data for this specific optical configuration is limited; process recipes are therefore tuned by measuring preform refractive index profiles and exhaust system pressure drop.

    When SiF₄ Replaces Silane, Silicon Tetrachloride, or Carbon Tetrafluoride

    Unlike silane or silicon tetrachloride, SiF₄ occupies a narrow precursor position among electronic silicon and fluorine sources. Compared with silane, SiF₄ is non-pyrophoric and does not supply hydrogen; this is advantageous in fluorinated glass deposition where Si-H bonds create optical absorption and where excess hydrogen can reduce film density. Silane remains preferred for polysilicon and silicon nitride because SiF₄ cannot deliver the reducing chemistry needed for silicon nucleation. Compared with silicon tetrachloride, SiF₄ is a gas at ambient temperature and can be delivered directly by mass flow control, whereas SiCl₄ requires bubbler or vaporizer systems and introduces chlorine. Chlorine contamination in films shifts transistor turn-on characteristics; fluorine, at controlled levels, reduces dielectric constant. Compared with carbon tetrafluoride, SiF₄ provides both silicon and fluorine and is used primarily for deposition rather than anisotropic plasma etching. Carbon tetrafluoride has a 100-year global warming potential of 6,630 according to IPCC AR6 and a long atmospheric lifetime; SiF₄ is consumed in hydrolysis and is not listed among the regulated perfluorocarbon greenhouse gases under the Kyoto Protocol.

    Table 2. Comparative handling and application properties of electronic silicon and fluorine sources
    PropertySiF₄ Electronic/ELSiH₄SiCl₄CF₄
    Phase at 21 °CCompressed gasPyrophoric gasLiquidCompressed gas
    Silicon deliveryYes, with fluorineYes, with hydrogenYes, with chlorineNo
    Primary electronic useFSG deposition, optical claddingPolysilicon, SiN, SiO₂SiO₂ coatings, fiber preformsPlasma etching
    Hydrolysis productHF + SiO₂SiO₂ + H₂HCl + SiO₂None
    Critical impurity controlH₂O ≤ 1 ppmvO₂ ≤ 1 ppmvChloride and metal contentN₂/O₂ and PFC abatement

    Because the compound hydrolyzes rapidly, handling boundaries for Electronic/EL SiF₄ are set by hydrogen fluoride formation and silica deposition. Scrubber systems should use a water scrubber followed by acid neutralization; scrubber solution pH should be maintained above 7 and below 9 to avoid silica scale on packing media. Gas detection sensors in storage and process areas should be calibrated for hydrogen fluoride and silicon tetrafluoride using gas standards prepared according to ISO 6142-1. Incompatibilities include water-saturated materials, ammonia, amines, and strong alkali; elastomeric seals should be limited to perfluoroelastomer grades validated for hydrogen fluoride service. Moisture ingress above 10 ppmv in the delivery line has been observed in production installations to form nonvolatile silica particles that block mass flow controller bypass filters and downstream gas distribution plates. Process tools should therefore be equipped with point-of-use purifiers and heated purge capability, and process abatement should be confirmed before line opening.

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